CROSS-REFERENCE TO RELATED PATENT APPLICATIONS
FIELD OF THE INVENTION
[0002] The present invention relates generally to tissue augmentation, and more particularly
to injection of resorbable, biocompatible, gel and solid composites to correct and
augment soft tissue with specific application for cosmetic augmentation of tissues.
BACKGROUND OF THE INVENTION
[0003] There are a number of non-resorbable, particle-based compositions used for permanent
correction or augmentation of soft tissue defects or augmentation for cosmetic purposes.
Each composition is associated with certain advantages and disadvantages. Silicone
gel was frequently used to treat dermal defects, such as wrinkles, folds, and acne
scars in the 1970's and 1980's but has since been prohibited from use in these applications.
Silicone was frequently associated with chronic inflammation, granuloma formation,
and allergic reactions. TEFLON® paste is a suspension of polytetrafluoroethylene particles
in glycerin. This composition was primarily used for vocal fold augmentation and has
been associated with granuloma formation. Bioplastics composed of polymerized silicone
particles dispersed in polyvinylpyrrolidone. This composition has been withdrawn from
commercial application due to frequent chronic inflammation and tissue rejection.
Polymethylmethacrylate (PMMA) microspheres having a diameter of 20-40µm and suspended
in a bovine collagen dispersion have been described by
Lemperle (U.S. Patent No. 5,344, 452). Since the composition contains collagen from a bovine source, skin testing is required.
In addition, the composition is associated with sterilization challenges; the bovine
collagen dispersion is damaged by standard terminal sterilization techniques, including
heat and gamma irradiation. PMMA is also labile to heat sterilization conditions.
[0004] Carboxymethylcellulose and other polysaccharides are examples of material used in
gel or solution form for a variety of medical and non-medical applications. Sodium
carboxymethylcellulose ("CMC") is cellulose reacted with alkali and chloroacetic acid.
It is water soluble and biodegradable and used in a number of medical and food applications.
It is also commonly used in textiles, detergents, insecticides, oil well drilling,
paper, leather, paints, foundry, ceramics, pencils, explosives, cosmetics and adhesives.
It functions as a thickening agent, a bonder, stabilizer, water retainer, absorber,
and adhesive.
[0005] The prior art gel materials teachings treat the gel merely as a carrier, incidental
to the actual augmentation function of the gel; and there has been no directed effort
to understanding how best to prepare an implant which is truly compatible rheologically
and chemically with an implant site. Further, conventional methods and products fail
to address several problems with current gels. More specifically, the injectable materials
of the prior art fail to address the specific difficulties in applying implants across
a wide range of locations in the body and consequently fail to provide the appropriate
type of implant. For example, current implants can experience occlusion, or irregular
implantation during the implantation procedure when a fine gauge needle is used. While
in certain applications a fine gauge needle may not be required, it is vital to the
success of several applications. In addition, a smaller gauge needle leaves a smaller
puncture point, which is often desirable to patients. Furthermore, the propensity
for occlusions often results in uneven, erratic and discontinuous implantation, which
causes highly undesirable results.
[0006] In another aspect of conventional methods and products, current implants have failed
to address the viscoelastic properties of the implant in the syringe, such that current
implants require a significant amount of force, and even irregular levels of force,
to extrude the implant from the needle, much more so as the needle gauge is reduced.
This presents fatigue issues for medical professionals who may well be performing
many injections in a day. This also makes any given injection more difficult to perform,
and also perform proper injection amounts and distributions, because of the necessity
to exert a large amount, or an irregular amount of force on the syringe, while maintaining
a steady needle during injection.
[0007] Conventional methods and current implant materials also fail to address the wide
range of distinctions in the different tissues in which the implants are placed. Implants
can undergo unwanted agglomeration, chemical reaction, phase separation, and premature
breakdown of the implanted mass into discontinuous variable shapes, all of which can
consequently manifest different undesirable mechanical properties and performance
relative to the implant tissue region.
[0008] Material composition and its associated mechanical, chemical, and even electrical
and other physical properties are important relative to: compatibility and stability
at the tissue implant site; controlled and proper tissue in-growth and to implement
integration into the tissue, immuno-histo tissue response, and mechanical and visual
appearance. The augmentation performance for the patient encompasses proper aesthetic
outcome arising from the function of the physical components and the chemical composition
of the composite of gel and particles implant. In particular, prior art implants utilizing
gels have relied on the gel as a carrier but have failed to recognize and solve the
problem of providing an implant with a gel which is designed to cooperate with the
solid particles to mimic, both mechanically and chemically, the tissue into which
it is injected and to behave in a symbiotic controlled manner when embedded in the
tissue.
SUMMARY OF THE INVENTION
[0010] The present invention is directed to systems and methods for preparation of implant
materials which enable compatible tissue augmentation. In particular, the systems
and methods relate to augmentation implants preformed in accordance with carefully
preparing implant matrix materials using a precise protocol to manipulate a plurality
of chemical variables to achieve a designed end product and with well define rheological
characteristics. In one embodiment, the implants comprise gels having specific compatibility
and stability at the tissue implant site; controlled and proper tissue in-growth to
implement integration into the tissue, minimized immuno-histo tissue response, and
improved mechanical and visual appearance. In one embodiment, the implant comprises
gels having particles suspended therein with specific compatibility and stability
at the tissue implant site; controlled and proper tissue in-growth to implement integration
into the tissue, minimized immuno-histo tissue response, and improved mechanical and
visual appearance. The implants have physical and chemical properties selected to
achieve a desired rheological and chemical behavior when implanted. For example, it
is preferable to replace or augment tissue structure with a material exhibiting physiological
properties, including rheological, chemical, biological, and mechanical properties,
which are similar, to and/or compatible with those of the treated tissue and/or designed
to accommodate tissue in growth in a controlled manner.
BRIEF DESCRIPTION OF THE DRAWINGS
[0011] FIG. 1 illustrates behavior of G' and G" for two different body tissue fluids;
[0012] FIG. 2 illustrates G' and G" for three different age body tissue fluids;
[0013] FIG. 3 illustrates a schematic method of manufacture of implant products;
[0014] FIG. 4 illustrates phase angle versus frequency behavior of lip tissue;
[0015] FIG. 5 illustrates Fo behavior versus viscosity for representative implant products
;
[0016] FIG. 6 illustrates a flow chart of an analytical statistical method to analyze chemical
variables to map to a target tissue rheology;
[0017] FIG. 7A shows a list of chemical variables and a tabular key for a first range of
rheological variables; FIG.7B(i) shows Fo versus percent CMC and viscosity; FIG. 7B(ii)
shows the same chemical variables versus G' at 0.7Hz; FIG. 7B(iii) same but for G'
at 4Hz; FIG. 7B(iv) same but for frequency response at 0.7Hz; FIG. 7B(v) same but
for tan δ at 0.7Hz; FIG. 7B(vi) same but for G" at 0.7Hz; FIG. 9B (vii) same but G"
at 4Hz; and FIG. 7B(viii) same but for frequency response at 4Hz; and FIG. 7C shows
the 2D plot of a region of rheological merit (white) versus a region not meeting the
parameters (dark);
[0018] FIG. 8 illustrates a flow chart of the steps in creating prediction profiles;
[0019] FIG. 9A(i) is a 3D contour of CMC percent versus PBS(mM) versus tan δ; FIG. 9A(ii)
is CMC versus PBS versus viscosity at 0.7Hz with planar cross-sections for FIG. 9B
shown; FIG. 9A(iii) is CMC versus PBS versus G' at 0.7Hz; FIG. 9A(iv) is CMC versus
PBS versus G" at 0.7Hz; FIG. 9A(v) is CMC versus PBS versus tan δ at 4Hz; FIG. 9A(vi)
is CMC versus PBS versus G' at 4Hz; FIG. 9A(vii) is CMC versus PBS versus G" at 4Hz;
FIG. 9A(viii) is CMC versus PBS versus frequency response at 0.7Hz; and FIG. 9(ix)
is CMC versus PBS versus frequency response at 4Hz; and FIG. 9B is a prediction profile
set and shows columns of rheological behavior for various chemical variables, each
taken from a cross-section from the contours of FIGS. 9A(i) - 9A(ix);
[0020] FIG. 10 illustrates a plot of elastic viscous modulus and complex viscosity as a
function of frequency for the composition of Example 1;
[0021] FIG. 11 illustrates a plot of elastic and viscous modulus and complex viscosity as
a function of frequency for the composition of Example 2;
[0022] FIG. 12 illustrates a plot of elastic and viscous modulus and complex viscosity as
a function of frequency for the composition of Example 3;
[0023] FIG. 13 illustrates a plot of elastic and viscous modulus and complex viscosity as
a function of frequency for the composition of Example 4;
[0024] FIG. 14 illustrates a plot of elastic and viscous modulus and complex viscosity as
a function of frequency for the composition of Example 5;
[0025] FIG. 15 illustrates a plot of elastic and viscous modulus and complex viscosity as
a function of frequency for the composition of Example 6;
[0026] FIG. 16 illustrates a plot of elastic and viscous modulus and complex viscosity as
a function of frequency for the composition of Example 7;
[0027] FIG. 17 illustrates a plot of elastic and viscous modulus and complex viscosity as
a function of frequency for the composition of Example 8;
[0028] FIG. 18 illustrates a plot of elastic and viscous modulus and complex viscosity as
a function of frequency for the composition of Example 9;
[0029] FIG. 19 illustrates a plot of elastic and viscous modulus and complex viscosity as
a function of frequency for the composition of Example 10;
[0030] FIG. 20 illustrates a plot of elastic and viscous modulus and complex viscosity as
a function of frequency for the composition of Example 11;
[0031] FIG. 21 illustrates a plot of elastic and viscous modulus and complex viscosity as
a function of frequency for the composition of Example 12;
[0032] FIG. 22 illustrates a plot of elastic and viscous modulus and complex viscosity as
a function of frequency for the composition of Example 13;
[0033] FIG. 23 illustrates a plot of elastic and viscous modulus and complex viscosity as
a function of frequency for the composition of Example 14;
[0034] FIG. 24 illustrates the viscosities for each of the materials as sheer rate varies;
[0035] FIG. 25 illustrates the loss modulus for each of the materials as sheer rate varies;
[0036] FIG. 26 illustrates the viscosity modulus for each of the materials as sheer rate
varies;
[0037] FIG. 27 illustrates the tan δ for each of the materials as sheer rate varies;
[0038] FIG. 28 demonstrates time dependency of the elasticity for varying gel compositions
with varying concentrations of particles (30% & 40% solids in 2.6 CMC: 1.5% glycerin
carrier vs. 30% solids in a 3.25% CMC: 15% glycerin carrier);
[0039] FIG. 29 illustrates the loss modulus G', the elastic modulus G" and tan δ (G'/G")
for compositions of Example 16;
[0040] FIG. 30 illustrates viscosity and tan δ properties for compositions of Example 16;
and
[0041] FIG. 31A shows a 3D desirability plot of glycerin versus Fo holding CMC and PBS constant;
FIG. 31B shows Fo versus PBS holding CMC and glycerin constant; FIG.31C shows PBS
versus CMC holding glycerin and Fo constant; FIG. 31D shows glycerin versus CMC holding
PBS and Fo constant; FIG. 31E shows Fo versus CMC holding PBS and glycerin constant;
and FIG. 31F shows glycerin versus PBS holding CMC and Fo constant.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
[0042] The present invention is directed to tissue augmentation implants and generally to
programmable rheology polysaccharide gels. More particularly, the invention relates
to polysaccharide compositions containing carboxymethylcellulose or other polysaccharide
polymers formulated to exhibit rheological characteristics which are designed particularly
to match the characteristics of the body tissue implant region of interest. For example,
the invention can be applied to provide tissue implant product throughout the body,
such as, for example, urinary tract, vocal fold, lip tissue, cheek, other dermal tissue
for various uses including clinical and restorative applications and cosmetic applications
like nasolabial folds, marionette lines, lip augmentation and wrinkles and folds.
In considering tissue augmentation implants, it is important to understand that physical
properties of body tissue are closely related to tissue function; and in one aspect
tissue cell response to the rheological characteristics (e.g., elasticity) of their
microenvironment must be properly accounted for. Understanding the physical structure
and function of tissues is of fundamental and therapeutic interest. It is therefore
most preferable to replace or augment tissue structure with a material exhibiting
physical properties, including rheological, and also chemical and biological properties
similar to those of the treated tissue. This provides improved tissue compatibility
of the implant material and encourages normal cell responsiveness. In addition, the
similar behavior of the implant and the surrounding tissue provides for a more natural
appearance to the augmented area and also can more readily accommodate controlled
tissue in-growth. The particular way in which the "similarity" of the implant rheology
is determined and control of the product manufacture are important aspects of the
invention. The details of the selection of the chemical and thermal treatment variables
for the implant product and their mapping to appropriate rheological values will be
described in detail hereinafter. Different tissues exhibit unique biomechanical and
chemical characteristics associated with tissue functions; and the effects of tissue
properties should be considered when augmenting or replacing these tissues. Consequently,
the implant products are formulated to achieve the desired rheological properties
to achieve tissue compatibility, as well as avoid unwanted chemical reactions and
phase separation.
[0043] Carboxymethylcellulose ("CMC") and other polysaccharides are examples of material
used in gel or solution which are used for a variety of medical and non-medical applications.
Sodium carboxymethylcellulose ("NaCMC") is cellulose reacted with alkali and chloroacetic
acid. It is one of the most abundant cellulose polymers available. It is water soluble
and biodegradable and used in a number of medical and food applications. It is also
commonly used in textiles, detergents, insecticides, oil well drilling, paper, leather,
paints, foundry, ceramics, pencils, explosives, cosmetics and adhesives. It functions
as a thickening agent, a bonder, stabilizer, water retainer, absorber, and adhesive.
[0044] A number of literature references describe carboxymethylcellulose and other ionic
polysaccharides as being viscoelastic and pseudoplastic.
See, for example: (
Andrews GP, German SP, Jones DS., Rheological Characterization of Primary and Binary
Interactive Bioadhesive Gels Composed of Cellulose Derivatives Designed as Ophthalmic
Viscosurgical Devices, Biomaterials. 2005 Feb;26 (5): 571-80;
Adeyeye MC, Jain AC, Ghorab MK, Reilly WJ Jr., Viscoelastic Evaluation of Topical
Creams Containing Microcrystalline Cellulose/sodium Carboxymethyl Cellulose as Stabilizer,
AAPS PharmSciTech. 2002; 3 (2): E8;
Lin SY, Amidon GL, Weiner ND, Goldberg AH., Viscoelasticity of Anionic Polymers and
Their Mucociliary Transport on the Frog Palate, Pharm. Res. 1993, Mar: 10 (3): 411-417;
Vais, AE, Koray, TP, Sandeep, KP, Daubert, CR. Rheological Characterization of Carboxymethyl
cellulose Solution Under Aseptic Processing Conditions, J. Food Science, 2002. Process
Engineering 25: 41-62).
[0045] The Aqualon Product Information publication from Hercules, Inc. describes the effects
of various parameters on rheology of sodium CMC. Viscosity increases with increasing
concentration, and CMC solutions are pseudoplastic and viscoelastic. Exposure to heat
results in a reduction in viscosity and effects are reversible under normal conditions.
After long periods of time, CMC will degrade at elevated temperatures with permanently
reduced viscosity. For example, moderate MW (Aqualon 7L) CMC heated for 48 hours at
180°F will lose 64% of viscosity. CMC is relatively stable to changes in pH and effects
of pH on viscosity are minimal in the physiologically relevant range of pH 6-9. There
is some loss of viscosity above 10 and some increase below 4. Salts may also affect
rheology of CMC; and monovalent cations interact to form soluble salts. If CMC is
dissolved in water and then salts are added, there is little effect on viscosity.
If CMC is added dry to salt solution, the viscosity can be depressed through ionic
repulsion. Polyvalent cations will not generally form crosslinked gels. Viscosity
is reduced when divalent salts are added to CMC solution and trivalent salts precipitate
CMC.
[0046] As can be concluded from consideration of the prior art, rheological and chemical
properties of the implant involve many complex factors. As such, one can vary each
of those components of the implant in order to design an implant with specific controlled
in vivo properties. Such degrees of freedom are in fact so large and complex that
designing the proper implant is a formidable task.
[0047] In order to resolve these complex tasks, it is instructive to consider the rheology
of selected body tissue components. Shown in FIG. 1 are two different body tissue
fluids composed of the same basic hyaluronic acid (sometimes referred to as hyluronic
acid) component but that show significantly different storage and loss modulus under
the same physiological strain conditions. Both solutions demonstrate shear thinning
and the material conversion from a viscous material (G" predominant or Tan δ >1) to
an elastic material (G' dominant) over a relatively small physiological shear stress
of 0.1 to 180 radians/sec (0.159Hz to 28.6Hz).
[0048] For example, it has been demonstrated that physiological fluids conform to the stress
imposed on them in varying ways. Dominant characteristics of a material can change
from a viscous lubrication material to elastic anchoring character as outside forces
are imposed. Shown in FIG. 2 are three of the same body tissue fluids composed of
the same basic hyaluronic acid component but that show significantly different storage
and loss modulus under the same physiological strain conditions based on the age of
an individual. The materials labeled "young" and "old" demonstrate shear thinning
and the material conversion from a viscous material (G" predominant or tan δ > 1)
to an elastic material (G' dominant) over a relatively small physiological shear stress
of 0.1 to 180 radians/sec. Material cross-over (G" = G') and relative amplitude is
dependent on age. The material labeled "osteoarthritis" did not cross-over under the
same shear conditions and the storage G' and loss modulus G" amplitudes were significantly
less than the other two materials. Therefore, it is demonstrated herein through formulation
and physical manipulation of the cellulose based implant that biologically relevant
biomechanical gel properties can be manufactured that can be tailored for the specific
application required. It is thus important to recognize this type of transition point
for biological acceptance of materials. Various controlling parameters, such as implant
product parameters can be manipulated, including buffer strength (such as PBS), polysaccharide
choice and concentration (such as NaCMC), lubricant content (such as glycerin); and
autoclave time can also be manipulated so that mechanical outputs of viscosity and
elasticity may be adapted to the desired outcome without creating all of the problems
apparent in the prior art.
[0049] For example, in one preferred embodiment of the present invention the method of manufacture
and product are directed to implants for tissue augmentation of the lips. As stated
earlier, physical properties of body tissue are closely related. Cellular propagation,
cellular infiltration and cellular function during tissue repair has been shown across
several cellular models to be dependent on the rheological characteristics (e.g.,
elasticity) of their microenvironment. As described hereinbefore, understanding the
physical structure and function of tissues is of fundamental therapeutic interest
during tissue augmentation and repair. It is therefore preferable to replace or augment
tissue structure with a material exhibiting physical properties, including rheological,
as well as chemical, biological, and mechanical properties, similar to those of the
treated tissue. The implants therefore provide an opportunity to match the properties
of the implant with that of the tissue in which the implant is to be placed. This
provides improved tissue compatibility of the implant material and encourages normal
cell responsiveness designed to provide controlled tissue in growth. In addition,
the similar behavior of the implant and the surrounding tissue provides for a more
natural appearance to the augmented area.
[0050] In one most preferred embodiment, the implant comprises gels of 2.6% CMC with 1.5%
glycerin in a 25mM phosphate buffer (PBS) at 7.4 pH. The phase angle ranged from 48
degrees to 140 degrees over the frequency range of 0.1 Hz to 10Hz. This is consistent
with published measurements for experimentally measured phase angle for the oblicularis
oris superior and inferior under voluntary stimulation where the phase angle ranged
from near 0 degrees to 150 degrees over the frequency range of 0.1Hz to 10Hz.
[0051] The magnitude of the initial phase angle is larger for the implant as the material
demonstrates more viscous character at f < 0.05. However, the material G'=G" cross-over
is 0.2; and the elastic character starts to dominate so as to simulate the elastic
behavior which has been experimentally measured in the art. For both the experimentally
measured and the proposed implant the phase angle demonstrates little change over
the frequency range of 0.1Hz to 1Hz with similar phase shifts noted over the same
biologically relevant ranges.
[0052] In one embodiment, the implant comprises gels of 2.6% CMC with 1.5% glycerin in a
25mM phosphate buffer at 7.4 pH with 30% v/v 25um to 45um calcium hydroxylapatite
particles. The material rheology is similar to the tissue site, especially at low
frequencies where the phase angle is linear. The material tests as an elastic material
over the frequency range. However, the tan δ starts at 0.9 (approximately G'= G")
and decreases as the material shear thins over the physiologically relevant range
of 0.1Hz to 10Hz.
[0053] It is also useful to understand certain terminologies used herein; including "rheology",
which is the study of the deformation and flow of matter. "Newtonian fluids" (typically
water and solutions containing only low molecular weight material), the viscosity
of which is independent of shear strain rate and a plot of shear strain rate. Non-Newtonian
fluid is a fluid in which the viscosity changes with the applied shear force. The
rheological outputs that describe a material are typically η, G', G", tan δ, deflection
angle relative to a linear force (shear) or oscillating force (Hz) of activity on
the tissue at an implant site. The parameter η is the viscosity, which is an indication
of the materials measure of the internal resistance of a material to deform under
shear stress. For liquids, it is commonly perceived as "thickness", or resistance
to pouring. G' is the storage modulus, which is an indicator of elastic behavior and
reveals the ability of the polymer system to store elastic energy associated with
recoverable elastic deformation. G" is the loss modulus, which is a measure of the
dynamic viscous behavior that relates to the dissipation of energy associated with
unrecoverable viscous loss. The loss tangent (tan δ) is defined as the ratio of the
loss modulus to the storage modulus (G"/G') and is dimensionless. It is a measure
of the ratio of energy lost to energy stored in a cycle of deformation and provides
a comparative parameter that combines both the elastic and the viscous contribution
to the system. A tan δ greater than 1 means the fluid is more liquid. A tan δ less
than 1 means the fluid is more solid. Deflection angle is defined as the angle from
a steady state after a force is applied to a material. The physiologically relevant
range of shear force and oscillation force is the body tissue activity range for typical
human function for that tissue. These ranges will be particularly evident, if a target
implant is directed to soft dermal tissue, dense collagenous tissue, muscle or bone.
[0054] The biomechanical behavior of biomaterials can therefore be characterized by measuring
their rheological properties. Rheology is related to viscoelasticity and viscoelastic
shear properties. Viscoelastic shear properties are quantified by complex shear modulus
which includes elastic shear modulus and viscous shear modulus. The magnitude of the
complex shear modulus has been used to indicate overall shear elasticity, stiffness,
and rigidity. If a material is purely elastic, then tan δ = 0. If the material is
purely viscous, the tan δ = infinity. All tissues exhibit a tan δ between these two
extremes.
[0055] Different tissues exhibit unique biomechanical characteristics associated with tissue
functions and the effects of tissue properties should be considered when augmenting
or replacing these tissues. This invention describes compositions that are formulated
to simulate the biomechanical properties of the tissues in which the compositions
are injected or implanted and avoid unwanted chemical reactions and phase separation.
Many different variables together provide the overall mechanical, chemical and biologic
properties of the implant. As such, one may vary each of those components of the implant
in order to design an implant with specific controlled in vivo properties. Sterility
is a necessary design requirement. Therefore, the sterilization mode and parameters
associated with the sterilization process are vital to the material design because
the intended use of the material is for tissue augmentation or replacement.
[0056] The implant is a composite injectable into soft tissue. The composite material comprises
a biocompatible gel with or without particles. Prior to and during injection, the
gel functions, in part, as a carrier for particles which might be present. In vivo,
the gel forms an integral part of the implant, providing the necessary pre-selected
mechanical and chemical microenvironment previously described for the implant to achieve
the desired article of manufacture.
[0057] As stated hereinbefore, the carrier preferably includes a polysaccharide gel wherein
the polysaccharides that may be utilized in the present invention include, for example,
any suitable polysaccharide and combinations thereof, within the following classes
of polysaccharides: celluloses/starch, chitin and chitosan, hyaluronic acid, hydrophobe
modified systems, alginates, carrageenans, agar, agarose, intramolecular complexes,
oligosaccharide and macrocyclic systems. Examples of polysaccharides grouped into
four basic categories include: 1. nonionic polysaccharides, including cellulose derivatives,
starch, guar, chitin, agarose and. dextron; 2. anionic polysaccharides including cellulose
derivatives starch derivatives, carrageenan, alginic acid, carboxymethyl chitin/chitosan,
hyaluronic acid and xanthan; 3. cationic polysaccharides, including cellulose derivatives,
starch derivatives guar derivatives, chitosan and chitosan derivatives (including
chitosan lactate); and 4. hydrophobe modified polysaccharides including cellulose
derivatives and alpha-emulsan. In one embodiment, the polysaccharide polymer is selected
from the group of sodium carboxymethylcellulose, hydroxyethyl cellulose, ethylhydroxyethyl
cellulose, carboxymethyl cellulose, carboxyethylhydroxyethyl cellulose, hydroxypropylhydroxyethyl
cellulose, methyl cellulose, methylhydroxylmethyl cellulose, methylhydroxyethyl cellulose,
carboxymethylmethyl cellulose, and modified derivatives thereof. Preferred polysaccharides
for use in the present invention include, for example, agar methylcellulose, hydroxypropyl
methylcellulose, ethylcellulose, microcrystalline cellulose, oxidized cellulose, chitin,
chitosan, alginic acid, sodium alginate, and xanthan gum. In certain embodiments,
more than one material may be utilized to form the gel, for example two or more of
the above listed polysaccharides may be combined to form the gel. In certain embodiments,
more than one material may be utilized to form the crosslinked gel, for example two
or more of the above listed polysaccharides may be combined to form the gel.
[0058] In addition, the gel may be crosslinked. Appropriate gel crosslinkers include for
example: heat, pH, and crosslinking through mono valent, di-valent, and tri-valent
cationic interactions. The crosslinking ions used to crosslink the polymers may be
anions or cations depending on whether the polymer is anionically or cationically
crosslinkable. Appropriate crosslinking ions include, but are not limited to cations
selected from the group consisting of calcium, magnesium, barium, strontium, boron,
beryllium, aluminum, iron, copper, cobalt, and silver ions. Anions may be selected
from but are not limited to the group consisting of phosphate, citrate, borate, carbonate,
maleate, adipate and oxalate ions. More broadly, the anions are derived from polybasic
organic or inorganic acids. Preferred crosslinking cations are calcium iron and barium
ions. The most preferred crosslinking cations are calcium and iron. The preferred
crosslinking anions are phosphate, citrate and carbonate. Crosslinking may be carried
out by contacting the polymers with an aqueous solution containing dissolved ions.
Additionally, crosslinking could be accomplished through organic chemical modification
including: polyfunctional epoxy compound is selected from the group consisting of
1,4-butanediol diglycidyl ether (BDDE), ethylene glycol diglycidyl ether (EGDGE),
1,6-hexanediol diglycigyl ether, polyethylene glycol diglycidyl ether, polypropylene
glycol diglycidyl ether, polytetramethylene glycol digylcidyl ether, neopentyl glycol
digylcidyl ether, polyglycerol polyglycidyl ether, diglycerol polyglycidyl ether,
glycerol polyglycidyl ether, tri-methylolpropane polyglycidyl ether, pentaerythritol
polyglycidyl ether, and sorbitol polyglycidyl ether. Additionally, crosslinking could
be accomplished through organic chemical modification through the carbonyl or hydroxide
functionality of the polysaccharide backbone reaction. In embodiments utilizing more
than one type of polymer, the different polymers may crosslink with each other to
form further crosslinking.
[0059] As shown by the Example 19, the discussion regarding FIG. 9B, and data provided hereinafter,
in one embodiment the implant comprises a gel, the tan δ (ratio of the viscosity modulus
G" to the loss modulus G') of which can be manipulated by adjusting the concentration
of salt (in this case potassium phosphate or PBS) in NaCMC formulations that are subsequently
heat sterilized. In compositions prepared in water, the tan δ is <1 before and after
heat treatment, indicative of a elastic fluid. If the compositions are prepared in
dilute salt solutions, the tan δ is <1 before heat treatment and >1 after heat treatment.
A tan δ >1 generally indicates a viscous fluid. Both dilute salt (in this case monovalent)
and heat treatment are needed to convert the composition from a tan δ <1 to a tan
δ >1. As the salt concentration increases, the viscosity of the composition is reduced
by reducing the ability of the polysaccharide to internally crosslink.
[0060] In selected compositions for tissue augmentation a viscosity is preferred that will
provide some bulking capability in addition to satisfying tissue rheological behavior.
Therefore, the salt concentration is preferably carefully controlled at relatively
low levels, usually less than 100mM.
[0061] The addition of glycerin to salt solution reduces the tan δ, i.e., the composition,
even after heat treatment, remains elastic, because the rheological properties of
the glycerin provide bulking rheological interaction with the polysaccharide gel.
The tan δ is preferably and usually <1. However, the tan δ of this composition is
different from the tan δ of compositions prepared in water without salt. The rheological
characteristics of NaCMC can be manipulated by salt, glycerin, and heat treatment.
[0062] In addition to the desire to accommodate the rheological character of the implant
tissue site, the gel of the present invention can be adjusted to control extrusion,
decomposition rate (chemical and physical), moldability and porosity to modulate tissue
response. Gel characteristics also control varying rates of resorption, as host tissue
forms around the slower resorbing ceramic particles.
[0063] In one embodiment, the present invention provides a gel capable of supporting solid
particles for injection through fine gauge needles and forming an integral and compatible
part of the implant (and surrounding bio-environment) once injected. The implant includes
particles suspended in the gel. In certain embodiments, the particles are ceramic
based composites. Particulate ceramic materials include, but are not limited to, calcium
hydroxyapatite, and other suitable materials including, but are not limited to, calcium
phosphate-based materials, and the like. Examples include, but are not limited to,
tetracalcium phosphate, calcium pyrophosphate, tricalcium phosphate, octacalcium phosphate,
calcium fluorapatite, calcium carbonate apatite, alumina-based materials, and combinations
thereof. The ceramic particles may be smooth rounded, substantially spherical, particles
of a ceramic material embedded in a biocompatible gel material that is continuous,
crosslinked or in a dehydrated configuration as discussed below. In this embodiment,
particles may range in size 20 microns to 200 microns and preferably from about 20
microns to 120 microns and most preferably from 20 microns to 45 microns. Concentration
of ceramic particles ranges from 5% to 65%, by volume, preferably from 10% to 50%
by volume and most preferably from 30% to 45% by volume.
[0064] Particles which can be added to the gel can be made of a biocompatible but non-biodegradable
material. Suitable materials include glass, e-PTFE, PTFE, polypropylene, polyacrylamide,
polyurethane, silicone, polymethylmethacrolate, Dacron, carbon particles, TEFLON®,
metals of iron, copper nickel titanium alloys thereof including Nitinol, silver, gold,
platinum, or stainless steel. The particles can be comprised of a plurality of layers
of materials including organic polymers and proteins. Additionally, one can select
particles from organic biopolymers of elastomers such as, for example, acrylic polymers,
vinyl alcohol polymers, acrylate polymers, polysaccharides, the acrylic family such
as polyacrylamides and their derivatives, polyacrylates and their derivatives as well
as polyallyl and polyvinyl compounds. All of these polymers are crosslinked so as
to be stable and non-resorbable, and can contain within their structure other chemicals
displaying particular properties or mixtures thereof. The particles may preferably
include a polysaccharide particle, for example, any suitable polysaccharide and combinations
thereof, within the following classes of polysaccharides: celluloses/starch, chitin
and chitosan, hyaluronic acid, hydrophobe modified systems, alginates, carrageenans,
agar, agarose, intramolecular complexes, oligosaccharide and macrocyclic systems.
Examples of polysaccharides can be grouped into four basic categories and include:
1. nonionic polysaccharides, including cellulose derivatives, starch, guar, chitin,
agarose and. dextron; 2. anionic polysaccharides including cellulose derivatives starch
derivatives, carrageenan, alginic acid, carboxymethyl chitin/chitosan, hyaluronic
acid and xanthan; 3. cationic polysaccharides, including cellulose derivatives, starch
derivatives guar derivatives, chitosan and chitosan derivatives (including chitosan
lactate); and 4. hydrophobe modified polysaccharides including cellulose derivatives
and alpha-emulsan. In one preferred embodiment, the polysaccharide polymer is selected
from the group of sodium carboxymethylcellulose, hydroxyethyl cellulose, ethylhydroxyethyl
cellulose, carboxymethyl cellulose, carboxyethylhydroxyethyl cellulose, hydroxypropylhydroxyethyl
cellulose, methyl cellulose, methylhydroxylmethyl cellulose, methylhydroxyethyl cellulose,
carboxymethylmethyl cellulose, and modified derivatives thereof. Preferred polysaccharides
for use in the present invention include, for example, agar methylcellulose, hydroxypropyl
methylcellulose, ethylcellulose, microcrystalline cellulose, oxidized cellulose, chitin,
chitosan, alginic acid, sodium alginate, and xanthan gum. In certain embodiments,
more than one material may be utilized to form the particle, for example two or more
of the above listed polysaccharides may be combined to form the particle. In certain
embodiments, more than one, such as two or more polysaccharide materials can be utilized
in conjunction with those crosslinking agents previously listed herein, to form the
crosslinked particle. Further, particles, beads, microbeads, nanoparticles and liposomes
that may be suspended in gels may be porous, textured, coated, and solid surfaces
and can be round or other configurations.
[0065] These material compositions of the gel allow for better extrusion characteristics
through needle gauges as small as 27 to 30 gauge without the use of mechanical assistance
devices, and with less frequency of jamming or occlusion not previously accomplished
in prior art. While gels having particles suspended therein will clearly have different
extrusion characteristics than if there were no particles, the implants of the present
invention having particles suspended in gel exhibit improved extrusion over those
of the prior art. As particle size approaches that of the needle, extrusion becomes
increasing difficult. However, particle sizes below 75 microns allow for implants
of the present invention to be injected through fine gauge needs (such as 27 to 30
gauge). The gel is able to suspend the particles as a carrier and allow for less force
to extrude the implant with a lower likelihood of occlusion. Material compositions
with a higher tan δ in the range of 0.5 to 3.5 and most preferably between 0.5 and
2.0 demonstrate the best performance characteristic for extrusion through needle gauges
as small as 27 to 30 gauge. Material with higher tan δ are more preferable for instances
where mobility is the key parameter. Decreasing tan δ creates more stout, moldable
implant materials. Some examples of extrusion forces for CaHA loaded gel are in Table
1 below.
Table 1
| Physical parameters/ Material composition |
30% CaHA-3.25 CMC; 15% glycerin |
30% CaHA-2.6% CMC; 1.5% glycerin |
40% CaHA-2.6% CMC; 1.5% glycerin |
| Extrusion Force (lbf, 0.5" 27 Ga.) |
6.1 |
5.4 |
4.8 |
| Extrusion Force (lbf, 1.25" 27 Ga.) |
11.5 |
9.8 |
7.6 |
[0066] The preferred embodiment demonstrates substantially less required force than conventional
systems.
[0067] In one embodiment, the present invention provides a gel capable of supporting semi
solid particles for injection through fine gauge needles and forming an integral and
compatible part of the implant (and surrounding bio-environment) once injected. The
implant includes particles suspended in the gel. In certain embodiments, the particles
are excessively crosslinked polysaccharide based composites. Particulate materials
include, but are not limited to, CMC, agar and other suitable materials including,
but are not limited to, alginate, hyaluronic acid, chitosan and compositional combinations
of the like. Examples include, but are not limited to, hyaluronic acid/CMC, alginate/CMC
and chitosan/CMC ionically and chemically crosslinked combinations thereof. The particles
may be smooth rounded, substantially spherical, particles embedded in a biocompatible
gel material that is continuous, crosslinked or in a dehydrated configuration as discussed
below. In this embodiment, particles may range in size from about 20 microns to 200
microns, and preferably from 20 microns to 120 microns and most preferably from 20
microns to 45 microns. Concentration of particles ranges from 5% to 90%, by volume,
preferably from 10% to 80% by volume and most preferably from 60% to 70% by volume.
[0068] Furthermore, slight compositional changes in the gel carrier allows selection of
the biocompatibility parameters previously described, while still allowing for homogenous
particle suspension. Tissue specific proteins may be added to facilitate tissue response
either by acceleration (infiltration of extra cellular matrix or collagen) or decreasing
the immuno histological response. Such careful selection of these biocompatibility
characteristics enable achieving a preselected shape, cosmetic appearance, chemical
stability and bioenvironment to achieve stability of the implant or tissue in-growth
depending on the application. Increased biocompatibility and biomechanical capability
allows for the implant to degrade into compounds native to the body according to a
specific degradation profile.
[0069] In one embodiment, a decrease in glycerin content has provided for an improved osmolarity
range that is physiologically more similar to normal tissue physiological conditions
with improved biocompatibility not previously reported in the prior art. The preferred
form of the implant of the present invention does not rely on high amounts of glycerin
to suspend the particles, as prior art gels have done. Despite this, the gels of the
present invention are able to suspend a higher concentration of particles than previously
taught even in prior art gels which relied heavily on glycerin content. The decrease
in glycerin content enables the preferred embodiments to have a osmolarity range of
255mOs to 600mOs, preferable 255mOs to 327mOs, which is closer to the physiological
osmolarity of blood of 280 to 303mOs and is generally accepted as the range for cellular
compatibility. Control of the parameter is one degree of freedom in achieving the
above recited selection of a biocompatible implant. This preferred embodiment is described
in tabular form in Table 2.
Table 2
| Physical parameters/ Material composition |
30% CaHA-3.25 CMC; 15% glycerin |
30% CaHA-2.6% CMC; 1.5% glycerin |
40% CaHA-2.6% CMC; 1.5% glycerin |
| Osmolality (mmol/kg) |
1768 to 2300 |
291 |
289 |
[0070] This preferred embodiment is substantially more similar to normal physiological conditions
than any conventional product.
[0071] In addition, the decrease in glycerin and CMC allows for material rheologies of preferred
implant products that approach these physiological conditions or physiological conditions
of other extra cellular matrixes and bodily fluids. The lower viscosity modulus G"
and loss modulus G' allow for better tissue simulation at stress/strain amplitudes
typical to target tissue in the human body.
[0072] The decrease in glycerin content also enables the preferred embodiments to have a
water content range of 57.9% to 70.3%, which is closer to the physiological dermal
water content of 70% in embryonic skin to 60% in more mature skin. Materials that
are intended for tissue implantation that are closer to the physiological water content
of the target tissue create less osmotic stress to the tissues and cells immediate
to the implant.
[0073] Another controllable degree of freedom in constructing an implant to be biocompatible,
as explained in detail herein before, is control of CMC concentration. The decrease
in CMC concentration enables the preferred embodiments to have a thinner supporting
gel matrix which allows for more particle movement during the injection and post injection
which more closely mimics certain native tissue. It has been demonstrated that formulation
adjustment within the gel allows for increasing the bulking material composition while
still maintaining biologically relevant rheological characteristics. This facilitates
improved baseline correction and improved durability in the soft tissue corrections
while maintaining application standards consistent with the intended application.
This creates less regional tissue stress and strain which, in turn, limits the immuno
histological response in the form of erythema and edema thereby reducing recovery
time.
[0074] As stated hereinbefore, implants described herein may be used in many parts of the
body for tissue augmentation. For example, soft tissue that can be augmented by the
implant includes but is not limited to dermal tissue (folds and wrinkles), lips, vocal
folds, mucosal tissues, nasal furrows, frown lines, midfacial tissue, jaw-line, chin,
cheeks, and breast tissue. It will be appreciated that each of these areas exhibit
unique mechanical and biological properties. For example, the upper and lower lip
exhibit continuous mobility and require an implant that provides similar mobility
because of the muscle interaction and the decreased need for elasticity. Thus implants
exhibiting such characteristics provide for both a higher degree of biocompatibility,
mechanical compatibility, and a superior visual effect. As such, the implant may be
formulated so as to be specifically designed for implantation within a particular
portion of the body for addressing a particular indication. Table 3 illustrates the
tan δ for vocal folds and skin in the young and the elderly.
[0075] For typical dermis applications outside the face, the rheological response for characterization
may be better defined by G', G" or tan δ. This is summarized in Table 3 below, and
these particular rheological parameters are preferably used to define regions of merit
or volumes in desirability plots described hereinafter.
Table 3: Tan δ for Intact Tissues
| Tissue |
Tan δ |
Reference |
| Vocal fold (human) |
0.1-0.5 |
Chan, RW and Titze, IR. 1999. J. Acoust. Soc. Am., 106:2008-2021 |
| |
(0.2-0.5 at low frequency) |
| |
(0.1-0.3 at high frequency) |
| Human Dermis-23 year old |
0.61 |
Estimated as ratio of slopes of viscous modulus to elastic modulus from incremental
stress-strain curves (Silver, FH, Seehra, GP, Freeman, JW, and DeVore, DP. 2002. J. Applied Polymer Science,
86:1978-1985) |
| |
(strain rate 10% per minute) |
| |
1.02 |
| |
(strain rate 1000% per minute) |
| Human Dermis-87 year old |
0.36 |
|
| |
(strain rate 10% per minute) |
See above |
| |
1.16 |
|
| |
(strain rate 1009% per minute) |
|
[0076] Examples of preferred parameters for selected material compositions are set forth
below in Table 4.
Table 4
| Physical parameters/ Material composition |
30% CaHA-3.25 CMC; 15% glycerin |
30% CaHA-2.6% CMC; 1.5% glycerin |
40% CaHA-2.6% CMC; 1.5% glycerin |
| Tan δ @ 0.5Hz, 2r 30degree C |
0.453 |
0.595 |
0.581 |
[0077] Materials with higher tan δ are more preferable for instances where mobility is the
key parameter. Decreasing tan δ creates more stout, moldable implant materials. The
preferred embodiment demonstrates closer physiological response than conventional
product materials.
[0078] For example, for addressing indications where the tissue exhibits lower viscosity,
such as the lips, an implant having a viscosity of between 100,000 centipoise and
300,000 centipoise at 0.5Hz with a tan δ between 0.5 and 1 may be used. Likewise,
for addressing indications where a higher viscosity implant is desired such as facial
contouring in the midfacial area or other areas where the implant preferably provides
structural support, an implant having a viscosity of between 300,000 centipoise and
600,000 centipoise with a tan δ between 0.5 and 1 may be used. This is summarized
in Table 5 below.
Table 5
| Physical parameters/ Material composition |
30% CaHA-3.25 CMC; 15% glycerin |
30% CaHA-2.6% CMC; 1.5% glycerin |
40% CaHA-2.6% CMC; 1.5% glycerin |
| Viscosity (η @ 0.5Hz) |
413750 |
202865 |
396585 |
| Tan δ @ 0.5Hz |
0.453 |
0.595 |
0.581 |
| Viscosity modulus (G' @ 0.5Hz) |
1478.60 |
678.32 |
1331.8 |
| Loss Modulus (G" @ 0.5Hz) |
671.69 |
404.30 |
773.23 |
[0079] The tan δ of human vocal fold tissue ranges from 0.1-0.5 indicative of an elastic
material (
Chan, RW and Titze, IR, Viscoelastic shear properties of human vocal fold mucosa:
Measurement methodology and empirical results". 1999, J. Acoust. Soc. Am. 106:2008-2021). The tan δ of human skin ranges from 0.36 (older skin) to 0.61 (younger skin) (Calculated
from stress-strain data-
Silver, FH, Seehra, GP, Freeman, JW, and DeVore, DP. 2002. J. Applied Polymer Science,
86:1978-1985). The tan δ for skeletal muscles exceeds 1.0 indicative of a viscous material. The
tan δ for hyaluronic acid ranges from 1.3 to 0.3 as the material demonstrates shear
thickening and transitions through tan δ equal to 1 between 1 and 8 rad/s (0.17 to
1.3Hz) ( Fung YC, 1993 "Biomechanics: Mechanical properties of living tissue", Second
edition, Springer-Verlag, New York, NY). This is important when designing a composition
to augment human lips (muscle). There is even a difference in stiffness (more elastic
according to Chan and Titze, et. al) between the upper and lower lips and between
males and females. The lower lip is stiffer than the upper lip and male lips are stiffer
than female lips (
Ho, TP, Azar, K, Weinstein, and Wallace, WB. "Physical Properties of Human Lips: Experimental
Theoretical Analysis", 1982. J. Biomechanics. 15:859-866). The present invention describes compositions that can be formulated to a rheology
(including tan δ) that more closely simulates the tissue into which the biomaterial
is placed.
[0080] Human lips are primarily composed of skeletal muscle surrounded by loose connective
tissue covered by stratified keratinized squamous (similar to the stratum corneum
of skin). There is a difference in the stiffness of the lower and upper lip. Many
references equate stiffness to elasticity. If lip tissue is similar to skeletal muscle,
lip tissue exhibits significant elasticity. However, a composition with a higher tan
δ may result in fewer lip nodules, a common problem with prior art implants. Tissue
responses to any implant depend on several factors including the chemical composition,
physical configuration and biomechanical characteristics of the implant material and
on the biomechanical forces of the micro environment of the host tissue. Prior art
CaHA/CMC compositions injected into tissues under increased mechanical stress produce
more collagenous tissue (which may lead to undesired tissue in-growth in certain applications)
than when implanted in tissues under less mechanical stress. Part of this response
is related to the viscoelasticity of the implant. An implant under continuous mechanical
stress will react differently depending on the viscoelastic properties of the implant.
A highly viscoelastic implant (low tan δ) will continuously undergo shear thinning
to a lower viscosity and "recoil" to the initial higher viscosity. This continuous
change in implant mechanics may "turn on" or signal host cells to become more active
and to produce more collagen than an implant exhibiting more viscous rheology (higher
tan δ). More viscous implants will not undergo the same level of mechanical flux compared
to more viscoelastic implants.
[0081] For prior art compositions, thick collagenous material has been observed to encapsulate
individual particles. The implant does form a continuous mass between muscle bundles
(looks like muscle bundles were pushed apart) and particles are surrounded by a thick
fibrous ring with thinner collagen units integrating between particles. In contrast,
it has been observed in dermis and mucosal areas that collagen integration appears
as a continuous weave between particles and not as a thick capsule around individual
particles. This thick collagenous material around individual particles is similar
to that observed in a lip nodule biopsy. This encapsulation is likely related to the
continuous biomechanical forces in lip muscle, the elasticity and cohesiveness of
the material, and accumulation between muscle bundles.
[0082] Thus, while not limiting the scope of the invention a composition with a higher tan
δ may reduce the incidence of early nodules (those apparently associated with initial
inflammatory response and foreign body response to engulf and remove CMC) and of later
nodules resulting from excess fibrous tissue surrounding CaHA particles. A less elastic
and lower viscosity composition can provide a smoother flowing and more intrudable
implant with reduced biomechanical motion to signal host cells, thereby resulting
in fewer nodules.
[0083] In addition to a base implant product and also selectively the use of filler materials,
such as ceramics like CaHA, any number of medically useful substances for treatment
of a disease condition of a patient can be added to the implant composition at any
steps in the mixing process. Such substances include amino acids, peptides, vitamins,
co-factors for protein synthesis; hormones; endocrine tissue or tissue fragments;
synthesizers; angiogenic drugs and polymeric carriers containing such drugs; collagen
lattices; biocompatible surface active agents, antigenic agents; cytoskeletal agents;
cartilage fragments, living cells such as chondrocytes, bone marrow cells, mesenchymal
stem cells, natural extracts, transforming growth factor (TGF-beta), insulin-like
growth factor (IGF-1); growth hormones such as somatotropin; fibronectin; cellular
attractants and attachment agents. In addition, lidocaine and other anesthetic additions
to the gel are in the range of 0.1 % to 5% by weight, more preferably 0.3% - 2.0%
and most preferably 0.2% - 0.5%.
Manufacture of a Preferred Embodiment
[0084] In order to carry out a proper design and manufacture of the implant material, rheological
parameters are selectively established to achieve an implant product targeted for
a particular tissue site. In order to describe this process in detail, reference will
be made to FIG. 3 which sets forth the method in a stepwise manner. In a first step
100, one selects a particular tissue site for the implantation. For example, tissue
sites can include lip tissue, dermis and harder tissue, such as muscle tissue. The
tissue sites can be characterized by their rheological response to stress over a range.
For lip tissue as shown in FIG. 4, there are three regions of activity. In Region
1 for an initial small stress (0.1Hz,), the phase angle, demonstrates the material
to be elastic or muscle-like ( range 0 to 5) and is linear in character. The larger
the initial phase angle, the less dominate the character of the muscle/tissue interaction
or the softer the tissue (such as dermis). In Region 2, the general increase in stress
results in limited phase angle change. Muscle contraction does not dominate the elastic
character of muscle and has not exceeded the muscle tissue elastic limit. In Region
3, the general increase in stress results in phase angle change. Stress starts to
dominate the elastic character of the muscle tissue limit. The physiologically relevant
range for stress is 0.1Hz to 10Hz. Optimization for dermal filler applications in
the lip require consideration of the movement of muscles and soft bulbous tissue.
Lip morphology is primarily directed by muscle interaction with soft tissue. Lip contractions
are controlled by small sets of muscle: tissue nodes in multiple planes and dimensions.
A dermal filler for the lip should then be most preferably viscoelastic. The material
should be viscous under smalls stresses and gradually become elastic. The elastic
character is essential so that the material stays where implanted. Amplitudes for
G' & G" should be within the physiological range of similar ECM polysacchrides (
See Fung YC, 1993 "Biomechanics: Mechanical Properties of Living Tissue", Second Edition,
Springer-Verlog, New York, NY) and may range from 10cps to 300cps. This is summarized in Table 6 below.
Table 6
| Physical parameters/ Material composition |
3.25 CMC; 15% glycerin |
2.6% CMC; 1.5% glycerin |
| G' Range 0.1Hz to 10Hz |
86cps to 530 cps |
21cps to 238 cps |
| G" Range 0.1Hz to 10Hz |
66cps to 262 cps |
26cps to 154 cps |
| Tan δ Range 0.1 Hz to 10Hz |
0.77 to 0.49 |
1.19 to 0.647 |
[0085] A material that maintains or more closely approximates the range of G' and G" values
would be preferred. The preferred embodiment demonstrates a response that is substantially
more similar to a normal physiological response than any conventional product.
[0086] In a second step 110, rheological properties of the selected tissue site are determined
and proper limits of these rheological properties should be established. Consequently,
data must be accumulated (either by direct experimental tests or by reference to published
data) to define the range of tissue rheology and behavior during its use.
[0087] In a next step 120, the implant material system is identified, and in general, it
is important to satisfy several requirements in order to achieve a desirable rheology
and avoid chemical breakdown or phase separation. Initially, it is desirable to select
a polysaccharide based gel that can establish good chemical stability in the body.
In addition, the gel can be combined with buffer and lubricants and properly sterilized
to enable creating an implant with acceptable rheological behavior over the parameters
of body tissue use. An example of one such preferred system includes a NaCMC polysaccharide
gel, a buffer such as PBS, and a lubricant, such as glycerin. The composite material
when sterilized achieves Fo values from about 22 and above and most preferably from
about 24-33 which provides a value of about 10
-6 sterility. The implant viscosity versus Fo is shown in FIG. 5.
[0088] Other implant components are also useful and would most preferably include other
polysaccharides which have been described before, such as, celluloses/starch, chitin
and chitosan, hyaluronic acid, hydrophobe modified systems, alginates, carrageenans,
agar, agarose, intramolecular complexes, oligosaccharide and macrocyclic systems.
In addition, any physiologically acceptable buffer can be employed, such as and not
limited to glycine, citrate, and carbonate. A lubricant can also be employed, such
as for example and not limited to, mineral oils and complex fatty acids. All these
components must be adjusted by applying rigorous manufacturing standards described
hereinafter which enable achieving the prescribed rheological parameter over the range
of use of the particular tissue site.
[0089] In a next step 130, the chemical parameters of the selected implant material are
varied to achieve a relatively broad range of rheological behavior. These chemical
parameters are selected to cover such a reasonably broad range to insure the downstream
analyzation process is able to identify the full range of useful chemical compositions
from among the universe of possibilities. As will be described and illustrated graphically
hereinafter, this broad set of chemical values enables analytical isolation of phase
zones or regions of merit where the chemical characteristics map to an implant material
having rheological behavior fitted to the selected recipient tissue site.
[0090] As noted hereinbefore, prior art implant products have serious deficiencies. For
example, in one type of polysaccharide gel based implant for lip tissue, the implant
tends to undergo chemical reaction or phase separation occurs, causing accumulation
in nodules causing an irregular bumpy appearance in the lip tissue. These and other
known products, as shown hereinafter, are outside the proper rheological phase zone
or region of merit. The known implants do not demonstrate viscous behavior over the
physiologically relevant ranges (about 0.1 - 10Hz for stress) and therefore do not
crossover G" = G' or tan δ >1. The prior art implants are thicker (i.e., more viscous)
and cause an increased inflammatory response as the body increasingly recognizes the
material as foreign hyaluronic acid. In yet another example of a prior art product,
the material is based on highly crosslinked hyaluronic acid or hyaluronic acid particles
which have G' and G" plots that do not cross-over resulting in a deficient implant.
[0091] After step 130, which includes identification of the chemical parameters and selecting
a broad range of chemical implant values, in step 140 test product specimens are prepared
over a broad range and their rheological character is determined. The matrix of rheological
values includes frequency responses as a function of frequency (registered as phase
angles), elastic modulus G'; viscosity modulus G"; tan δ (G'/G") and viscosity over
the body tissue variable range of interest. A comparative analysis between material
compositions can then be performed to isolate the phase region of merit by methods
described hereinafter.
[0092] As noted above, experimental data have been taken for a substantial matrix of chemical
variables and the end rheological parameters determined. Various experimental data
and the rheology contours and mathematical descriptons of boundary lines for meeting
the desired rheology are set forth in Example 19 hereinafter. The data were processed
using four basic inputs: CMC concentration, glycerin concentration, phosphate buffer
concentration and Fo values. The variation of Fo for several representative implant
products is shown in FIG. 5. In performing these complex calculations described below
and illustrated in several figures, the Fo has been set at the end points of about
22 and 33 using a 121°C sterilization cycle; but other temperatures and times can
be used to achieve the same Fo values; and the effect of all other chemical variables
can be determined to map the chemical variables to the targeted proper rheological
property or properties for a given tissue implant site. It is generally understood
that sterilizing material requires that a specific Fo be reached to ensure 10
-6 sterility claims for a product. The use of different combinations of sterilization
time and temperature were studied in a Getinge Ab, Sweden autoclave to optimizing
the sterilization process. Materials were autoclaved at 121°C for run cycles of 3mins.,
6mins., 12mins., and 30mins. Sterilization programs had sterilization efficacy (Fo)
equal to 22, 25, 28 and 33 respectively and the 10
-6 sterility was achieved. Materials were autoclaved at 124°C for run cycles of 4mins.,
7.5mins., and 11 mins. Sterilization programs had sterilization efficacy (Fo) equal
to 26, 36, 46 respectively. Materials were autoclaved at 127°C for run cycles of 0.5min.,
1.5mins., and 3mins. Sterilization programs had sterilization efficacy (Fo) equal
to 42, 49, 57 respectively.
[0093] Variations on rheological parameters used in the method of manufacture can also be
incorporated into the analytical methods used to achieve the desired implant rheology.
For example, tan δ = G"/G' and such interrelationships can permit simplification of
the analysis, such as for example, given knowledge of two of the three parameters
to determine the impact of the third variable on rheological parameters. As mentioned
hereinbefore, these may be a subset of rheological parameters of particular interest
to the selected tissue implant site which thus may not require achieving all the above-mentioned
rheological parameter values. In addition, one or more of the rheological parameters
may be substantially insensitive to variations in one or more of the manufacturing
variables (such as, for example, content of polysaccharide gel, buffer concentration,
autoclave Fo value and lubricant content). This would then allow preparing a product
mapping to the particular one or more rheological properties for the tissue.
[0094] In a next step 150 in FIG. 6, an analytical method is used to identify the precise
chemical variables needed to map to the desired rheological phase zone to achieve
the rheologically matched implant product for the particular tissue site. As stated
hereinbefore, in a preferred embodiment the sterilization was carried to a particular
range of Fo to achieve a commercially acceptable 10
-6 sterility state. Further, the Fo value increased linearly with all treatments until
the beginning of the cooling phase. The main effect of different sterilization temperatures
on the cumulative Fo curves was an increase in the slope of the curves with increasing
sterilization temperature (
see FIG. 5). It also is possible to use higher sterilization temperatures than usually
suggested in pharmacopeias and thus shorten the process time. This sterilization process
preferably corresponds to a Fo value range of about 22 to at least about 33, and these
values are also associated with a change in the degree of polymeric chain breakdown,
as well as achieving the desired sterility. However, this breakdown of polymeric chain
leads to an effect on the rheological parameters; and in the most preferred embodiment
the range of 24-33 has been characterized in terms of all the remaining preparation
variables to establish proper rheological phase zones or regions of merit within which
the implant product has the required rheological values to perform well at the tissue
implant site. The methodology can also readily be extended to determine the effect
of higher Fo values.
[0095] In this step 150, one preferred methodology for data analysis to identify the proper
implant chemistry is performed using the set of chemical values associated with each
data point to carry out a rigorous modeling procedure. Further details are set forth
in Example 20. This embodiment can also be described as a screening model by using
four inputs: CMC concentration, glycerin concentration, phosphate buffer concentration
and Fo values. For example, CMC was varied between 2.3 wt% and 2.9 wt% in 0.1% increments,
the glycerin content was set to 1.5 wt.%, the buffer was set to O.M, 25mM and 100mM
concentration. The model was then executed using two separate Taguchi array screening
models as described in Example 19.
Using JMP7.0 pull down menus, the following path was used in the SAS JMP ver. 2.0
software:
Open Data set\Analyze\fit model\
Select model inputs by highlighting: Fo, CMC concentration (%CMC),
Glycerin concentration (%Gly), PBS concentration (XmM).
Use macros and choose and/or effect screening to capture all interactions for inputs
Use linear least squares fitting for model regression
Use effect screening for report format
Run Model
Under linear least squares: (graphing options of outputs) Highlight prediction profiler
to graphically represent input interactions.
Use pull down menus for setting specification limits-optional
Optimization is based on specification limits used.
Desirability is a unit-less parameter based on desirability of how well a condition
meets the specification for the input condition. Desirability may be calculated for
each condition of the data set. A graphing of desirability allows for graphical display
of all conditions which meet specifications.
Highlight Contour profile to graphically represent 2D input/response interactions.
Highlight Surface profiler to graphically represent 3D input/response interactions.
Successive iteration of 2-D graphing base on two variables allows for iterative examination
of the self limiting output function. This is an exhaustive excersize and only the
limiting condition plot is presented. Under this evaluation the sterilization time
was found to be limiting from 12 to 25 min (Fo 22 to 33).
[0096] The limiting value of Fo was then incorporated into the development of the prediction
model using the prediction formulas from the screening model contours for each output.
The screening model was developed based on the following four inputs: CMC concentration
(%CMC), glycerin concentration (%gly), phosphate buffer concentration (mM) and autoclave
time. The CMC concentration (%CMC) was varied between 2.3% w/v and 2.9% w/v in 0.1%
w/v increments. The glycerin concentration (%gly) was held to 0% w/v, 1.0% w/v and
1.5% w/v. The buffer concentration (mM) was varied from 0, 25mM, 50mM and 100mM concentration.
This creates a full factorial design of with 420 interative conditions. The prediction
formulas were input into a full factorial design. The rheological outputs were calculated
based on screening model prediction formulas.
See attachment II. Again, the data were analyzed by use of SAS JMP ver. 7.0 statistical
software following the steps of FIG. 6 to generate prediction profiles, three dimension
("3D") surface contour plots (
see, for example, FIG. 7B(i) - 7B(viii). The prediction model provides statistical strength
to the model incorporating more data points into the model description. Further details
are set forth in Example 19.
[0097] Again noted hereinbefore, the analysis by use of SAS JMP ver. 7.0 statistical software
provides useful three dimensional ("3D") contour plots (
see, for example, FIGS. 7B(i) - 7B(viii)) FIG. 7C and also FIGS. 9A(i) - 9A(ix). Other
suitable conventional statistical analysis software can also be used in this one type
of methodology to analyze the base chemical parameter data from the test product samples.
This approach can generate data fits allowing formation of 3D surfaces and line fits
to identify phase regions of merit based on the implant/tissue constraints to determine
the three dimension plot of rheological behavior and selection of a minimum and maximum
range of those rheological parameters to meet the preset desired rheological conditions
and properties. Example 19 hereinafter also provides details of equations defining
the boundary lines and contours.
[0098] Regarding criteria for rheological variables for the implant product, Example 19
is for an implant application in lip tissue, wherein (1) the G' and G" behavior should
preferably be within a range of about 0 to 300pas to map to the desired property since
the interstitial extracellular matrix of the lip tissue comprises a hyaluronic acid
polysaccharide for which the rheology range can be identified; and their plots should
crossover at a physiologically relevant frequency of about .5 to 4Hz which is consistent
with the lip tissue functionality, and (2) the viscosity should be about 0 to 300,000cps
for the same physiologically relevant stress ranges. The tan δ should be greater than
1 for low stress conditions indicating an inherent viscous nature to the material
with decreasing tan δ as the stress increases demonstrating elastic behavior of lip:tissue
nodal properties. Phase or deflection angle should be about 5 to 110 over the stress
range of 0.1Hz to 4Hz. The SAS analytical method produced families of rheological
variable plots that met the following rheological evaluation parameters and can be
summarized in Table 7.
Table 7
| Rheological parameter |
|
|
| Viscosity ( 5τ, 30 degree C parallel plate ) 0.7Hz |
7200cps to 53000 cps |
Data based on the specification limits of a present conventional implant product.
This is supported in the published references for several hyaluronic acid compositions. |
| Tan δ 0.7Hz |
> 1 |
Data based on the specification limits of the conventional product and the desired
rheology at low stresses. Material for dermal application should show minimal elastic
behavior at low stress to act more like the surrounding tissue and the Newtonian fluid
(water) microenvironment. This is supported in the published references for several
hyluronic acid compositions as they demonstrate viscous to elastic behavior under
increasing stress and cross-over at some stress point. |
| G" and G" 0.7Hz |
<300cps |
Data from Fung reference with various hyaluronic acid compositions. Hyaluronic acid
is a primary constituent of dermal extra cellular matrix. |
| G' and G" 4.0Hz |
< 100cps |
Data from Fung reference with various hyaluronic acid compositions. Hyaluronic acid
is a primary constituent of dermal extra cellular matrix and this seems to be applicable. |
| Tan δ 11.7Hz |
<1 |
Data set based on the specification limits of the conventional product and the desired
rheology at higher stresses. It would be best if material demonstrated some elastic
character when subjected to higher stress to limit movement or deformation of form. |
| δ- R 0.7Hz & 4Hz |
< 60 and <110 |
Data supported in published references for phase angle evaluation of lips. The limits
were subjective and taken from the graphs as presented in the literature. Evaluation
at two points 0.7Hz & 4Hz covers the physiologically relevant range of stresses. |
[0099] In a next step 160, lines having a mathematical behavior are part of a series of
identified loci for each single one of the rheological variables for which the conditions
have been met. These are shown in FIG. 7C as the line separating the acceptable white
zone from the adjacent dark zone. As stated hereinbefore Example 19 provides further
details of the analysis and the mathematical descriptions. Also in a step 170, a phase
zone of merit can be identified which is the white zone in FIG. 7C where the universe
of rheological parameters limits were all met. This establishes the target implant
product phase zone of merit. In some cases, as noted hereinbefore, it is necessary
to use only one of the rheological parameters to define a "region of merit" in order
to identify the chemical characteristics which meet the implant tissue requirements.
Numerous examples are set forth hereinafter delineating these rheological loci of
proper performance or merit and also target rheological phase zones of merit. The
examples are in particular directed to lip tissue implantation; but in view of knowledge
of other tissue rheology, the methodology described herein can be used for any tissue
site with known rheological parameters. The statistical method is executed by the
above-referenced SAS off the shelf software formalisms, including for example Monte
Carlo calculations and which are part of the analysis show in the statistical analysis
flow chart of FIG. 3.
[0100] In another embodiment, an enhancement based on the steps 160 and 170 can be implemented
to establish the applicability and functionality of the rheological variables relative
to the chemical variables. This can be accomplished by a step 180 of generating a
predictive profiler mathematical model using the one or more inputs of the rheological
parameters in a screening model least squares regression to form plots of chemical
variables versus rheological outputs of choice. FIG. 8 shows the steps of the predictive
profiler in step 181 of implementing the screening model of step 150 to select one
of the rheological parameters as a function of two chemical variables. From this analysis
the SAS software can generate in step 182 the 3D contours of the rheological parameters
versus the two chemical variables (
see, for example, FIGS. 9A(i)) - 9A(ix)). In a next step 183 a planar cross-section is
taken at a set value of one of the chemical variables (
see FIG. 9A(ii)). In a next step 184, the planar intersection with the contour of the
rheological function establishes a line for the selected variables (
see FIG. 9B for a matrix of these various lines in the rheology contours for the given
parameters). In a step 185 knowledge of the sensitivity of the rheology parameters
to the chemical variables allows control of the chemistry. (
See the various plots in FIG. 9B). These prediction profiles then demonstrate how the
change in one chemical variable input has a fairly modest impact on certain rheological
variables as the other variables are held constant, while other chemical variables
have very dramatic impact on rheological response as the other variables are held
constant. For example, as shown in FIG. 9B, the PBS chemical variable causes quite
dramatic changes in selected rheological outputs. Their variability (or lack thereof)
can be used to either simplify manufacture of a desired end product or further effect
the ultimate value of a given rheological variable in combination with knowledge of
the location within a rheological phase zone or region suitable for a selected tissue
implant site. As described hereinbefore, further details of the mathematical equations
which are created by the SAS software to describe contours and lines are characterized
in Example 19 and are executed by graphing scripts of the software.
[0101] In another procedure in step 190, a "desirability" measure or region can be determined
by analyzing the input data and rheological parameters by limiting the model to only
those conditions which meet the required output ranges. Desirability is an index to
evaluate if the testing condition meets the specifications and to what degree. Those
values that are less than 0 fail to meet one or all of the criteria for acceptable
material. Thus they are not included in the 3D plots. All other combinations of variables
that have positive desirability meet the specification goals to some relative degree.
The threshold condition of desirability was limited to 0.5 as the predictive optimal
obtainable in this case (as no one condition optimizes all outputs). Model strength
can be further enhanced by increasing the amount of experimental data. This can be
done through the brute force method of more iterative runs of all possible conditions
or in this case the statistical SAS JMP ver. 7.0 included a Monte Carlo simulation
to infinitely limit the degree of acceptable material, therefore defining the surface
of the acceptable region. A threshold limit for desirability was established at 0.15
to allow a degree of confidence in the model simulation because normal variance was
included in the Monte Carlo simulation.
[0102] The methods and products described hereinbefore can be implemented by a supplier
establishing a database of rheological data for tissue of any one of a plurality of
particular types of patients; and understanding how to execute the methods described
herein, the supplier can then map out implant products and their associated rheological
properties to determine which products meet the compatibility requirements for the
particular tissue. Thus, the above-described regions of merit and also desirability
plots can help define the proper product.
[0103] Examples of such a "desirability " analysis are provided hereinafter in FIGS. 31A-31F.
[0104] The following non-limiting examples illustrate various aspects of the invention.
Example 1
Preparation of 2.3% sodium CMC gel in sterile water.
[0105] Sodium carboxymethylcellulose was prepared in sterile water for injection and adjusted
to a pH of from about 7.1 to about 8.0 using potassium hydroxide. The dispersion was
mixed in an orbital Ross mixer @1725 RPM for 5 minutes followed by mixing in an orbital
Ross mixer @1725 RPM for 40 minutes, while holding a vacuum @26mm Hg or more. The
composition was then steam sterilization at 121°C for times ranging from 3 minutes
to 30 minutes. In addition, one sample was sterilized for time intervals between 3
minutes and 30 minutes @121°C. Results are shown in FIG. 10 where G' represents the
elastic modulus, G" represents the viscous modulus and η the complex viscosity. The
profile shows that G' and G" intersect at 0.495Hz (3.2 Rad/sec). Above this frequency,
the composition exhibits non-Newtonian solution characteristics (tan δ < 1.0).
Example 2
Preparation of 2.4% sodium CMC gel in sterile water.
[0106] Sodium carboxymethylcellulose was prepared in sterile water for injection and adjusted
to a pH of from about 7.1 to about 8.0 using potassium hydroxide. The dispersion was
mixed in an orbital Ross mixer @1725 RPM for 5 minutes followed by mixing in an orbital
Ross mixer @1725 RPM for 40 minutes while holding a vacuum @26mm Hg or more. The composition
was then steam sterilization at 121°C for times ranging from 3 minutes to 30 minutes.
In addition, one sample was sterilized for time intervals between 3 minutes and 30
minutes @121°C. Results are shown in FIG. 11 where G' represents the elastic modulus,
G" represents the viscous modulus and η the complex viscosity. The profile shows that
G' and G" intersect at .0299Hz (1.8 Rad/sec) (lower frequency than that shown in FIG.
1). Above this frequency, the composition exhibits non-Newtonian solution characteristics
(tan δ < 1.0).
Example 3
Preparation of 2.5% sodium CMC gel in sterile water.
[0107] Sodium carboxymethylcellulose was prepared in sterile water for injection and adjusted
to a pH of from about 7.1 to about 8.0 using potassium hydroxide. The dispersion was
mixed in an orbital Ross mixer @1725 RPM for 5 minutes followed by mixing in an orbital
Ross mixer @1725 RPM for 40 minutes, while holding a vacuum @26mm Hg or more. The
composition was then steam sterilization at 121°C for times ranging from 12 minutes
to 30 minutes. In addition, one sample was sterilized for time intervals between 3
minutes and 12 minutes @121°C. Results are shown in FIG. 12 where G' represents the
elastic modulus, G" represents the viscous modulus and η the complex viscosity. The
profile shows that G' and G" intersect at 0.157Hz (1 rad/sec) frequency than shown
in FIGS. 10 and 11. Above this frequency, the composition exhibits non-Newtonian solution
characteristics (tan δ < 1.0).
Example 4
Preparation of 2.6% sodium CMC gel in sterile water.
[0108] Sodium carboxymethylcellulose was prepared in sterile water for injection and adjusted
to a pH of from about 7.1 to about 8.0 using potassium hydroxide. The dispersion was
mixed in an orbital Ross mixer @1725 RPM for 5 minutes followed by mixing in an orbital
Ross mixer @1725 RPM for 40 minutes while holding a vacuum @26mm Hg or more. The composition
was then steam sterilization at 121°C for times ranging from 12 minutes to 30 minutes.
In addition, one sample was sterilized for time intervals between 12 minutes and 30
minutes @121°C. Results are shown in FIG. 13 where G' represents the elastic modulus,
G" represents the viscous modulus and η the complex viscosity. The profile shows the
G' and G" intersect at 0.164Hz (1.03 rad/sec). Above this frequency, the composition
exhibits non-Newtonian solution characteristics (tan δ < 1.0).
Example 5
Preparation of 2.3% sodium CMC gel in potassium phosphate buffer.
[0109] Sodium carboxymethylcellulose was prepared in sterile 25mM to 100mM potassium phosphate
buffer pH and adjusted to a pH of from about 7.2 to about 8.0 using potassium hydroxide.
The dispersion was mixed in an orbital Ross mixer @1725 RPM for 5 minutes followed
by mixing in an orbital Ross mixer @1725 RPM for 40 minutes while holding a vacuum
@26mm Hg or more. The composition was then steam sterilization at 121°C for times
ranging from 3 minutes to 12 minutes. In addition, one sample was sterilized for time
intervals between 3 minutes and 12 minutes @121°C. Results are shown in FIG. 14 where
G' represents the elastic modulus, G" represents the viscous modulus and η the complex
viscosity. The profile shows that G' and G" intersect at 2.401Hz (15 rad/sec) (similar
to that shown in FIG. 13). Above this frequency, the composition exhibits non-Newtonian
solution characteristics (tan δ < 1.0).
Example 6
Preparation of 2.4% sodium CMC gel in potassium phosphate buffer.
[0110] Sodium carboxymethylcellulose was prepared in sterile 25mM to 100mM potassium phosphate
buffer pH and adjusted to a pH of from about 7.2 to about 8.0 using potassium hydroxide.
The dispersion was mixed in an orbital Ross mixer @1725 RPM for 5 minutes followed
by mixing in an orbital Ross mixer @1725 RPM for 40 minutes while holding a vacuum
@26mm Hg or more. The composition was then steam sterilization at 121°C for times
ranging from 3 minutes to 12 minutes. In addition, one sample was sterilized for time
intervals between 3 minutes and 12 minutes @121°C. Results are shown in FIG. 15 where
G' represents the elastic modulus, G" represents the viscous modulus and η the complex
viscosity. The profile shows that G' and G" intersect at 1.56Hz. (9.8 rad/sec). Above
this frequency, the composition exhibits non-Newtonian solution characteristics (tan
δ < 1.0).
Example 7
Preparation of 25% sodium CMC gel in potassium phosphate buffer.
[0111] Sodium carboxymethylcellulose was prepared in sterile 25 mM to 100 mM potassium phosphate
buffer pH and adjusted to a pH of from about 7.2 to about 8.0 using potassium hydroxide.
The dispersion was mixed in an orbital Ross mixer @1725 RPM for 5 minutes followed
by mixing in an orbital Ross mixer @1725 RPM for 40 minutes while holding a vacuum
@26 mm Hg or more. The composition was then steam sterilization at 121°C for times
ranging from 3 minutes to 12 minutes. In addition, one sample was sterilized for time
intervals between 3 minutes and 12 minutes @121°C. Results are shown in FIG. 16 where
G' represents the elastic modulus, G" represents the viscous modulus and η the complex
viscosity. The profile shows that G' and G" intersect at 4.54Hz (28.5 rad/sec). Above
this frequency, the composition exhibits non-Newtonian solution characteristics (tan
δ < 1.0).
Example 8
Preparation of 2.6% sodium CMC gel in potassium phosphate buffer
[0112] Sodium carboxymethylcellulose was prepared in sterile 25mM to 100mM potassium phosphate
buffer pH and adjusted to a pH of from about 7.2 to about 8.0 using potassium hydroxide.
The dispersion was mixed in an orbital Ross mixer @1725 RPM for 5 minutes followed
by mixing in an orbital Ross mixer @1725 RPM for 40 minutes while holding a vacuum
@26mm Hg or more. The composition was then steam sterilization at 121°C for times
ranging from 3 minutes to 12 minutes. In addition, one sample was sterilized for time
intervals between 3 minutes and 12 minutes @121°C. Results are shown in FIG. 17 where
G' represents the elastic modulus, G" represents the viscous modulus and η the complex
viscosity. The profile shows that G' and G" intersect at 3.61 (22.7 rad/sec) Hz. Above
this frequency, the composition exhibits non-Newtonian solution characteristics (tan
δ < 1.0).
Example 9
Preparation of 2.7% sodium CMC gel in potassium phosphate buffer.
[0113] Sodium carboxymethylcellulose was prepared in sterile 25mM to 100mM potassium phosphate
buffer pH and adjusted to a pH of from about 7.2 to about 8.0 using potassium hydroxide.
The dispersion was mixed in an orbital Ross mixer @1725 RPM for 5 minutes followed
by mixing in an orbital Ross mixer @1725 RPM for 40 minutes while holding a vacuum
@26mm Hg or more. The composition was then steam sterilization at 121°C for times
ranging from 3 to 12 minutes. In addition, one sample was sterilized for time intervals
between 3 minutes and 12 minutes @121°C. Results are shown in FIG. 18 where G' represents
the elastic modulus, G" represents the viscous modulus and η the complex viscosity.
The profile shows that G' and G" intersect at 3.49Hz (21.9 rad/sec). Above this frequency,
the composition exhibits non-Newtonian solution characteristics (tan δ < 1.0). At
this sodium CMC concentration (2.7%) the intersect shifts to a lower frequency than
that shown in FIG. 16 (2.5% CMC). The composition still exhibits Newtonian fluid characteristics.
Example 10
Preparation of 2.8% sodium CMC gel in potassium phosphate buffer.
[0114] Sodium carboxymethylcellulose was prepared in sterile 25mM to 100mM potassium phosphate
buffer pH and adjusted to a pH of from about 7.2 to about 8.0 using potassium hydroxide.
The dispersion was mixed in an orbital Ross mixer @1725 RPM for 5 minutes followed
by mixing in an orbital Ross mixer @1725 RPM for 40 minutes while holding a vacuum
@26mm Hg or more. The composition was then steam sterilization at 121°C for times
ranging from 3 minutes to 12 minutes. In addition, one sample was sterilized for time
intervals between 3 minutes and 12 minutes @121°C. Results are shown in FIG. 19 where
G' represents the elastic modulus, G" represents the viscous modulus and η the complex
viscosity. The profile shows that G' and G" intersect at 4.88Hz (30.7 rad/sec). Above
this frequency, the composition exhibits non-Newtonian solution characteristics (tan
δ < 1.0). Since the intersect occurs at the top end frequency, this composition exhibits
Newtonian characteristics at nearly all frequencies.
Example 11
Preparation of 2.6% sodium CMC gel in potassium phosphate buffer and glycerin.
[0115] Sodium carboxymethylcellulose was prepared in sterile 25mM to 100mM potassium phosphate
buffer adjusted to a pH of from about 7.2 to about 8.0 using potassium hydroxide and
containing up to 1% glycerin. The dispersion was mixed in an orbital Ross mixer @1725
RPM for 5 minutes followed by mixing in an orbital Ross mixer @1725 RPM for 40 minutes
while holding a vacuum @26mm Hg or more. The composition was then steam sterilization
at 121°C for times ranging from 3 minutes to 12 minutes. In addition, one sample was
sterilized for time intervals between 3 minutes and 12 minutes @121°C. Results are
shown in FIG. 20 where G' represents the elastic modulus, G" represents the viscous
modulus and η the complex viscosity. The profile shows that G' and G" intersect at
1.254Hz (7.8 rad/sec). Above this frequency, the composition exhibits non-Newtonian
solution characteristics (tan δ < 1.0). The addition of glycerin to sodium CMC gel
in potassium phosphate significantly affects the rheology of the composition, changing
it from a fundamentally Newtonian fluid to a non-newtonian fluid above a frequency
of about 1.0.
Example 12
Preparation of 2.7% sodium CMC gel in potassium phosphate buffer and glycerin.
[0116] Sodium carboxymethylcellulose was prepared in sterile 25mM to 100mM potassium phosphate
buffer adjusted to a pH of from about 7.2 to about 8.0 using potassium hydroxide and
containing up to I % glycerin. The dispersion was mixed in an orbital Ross mixer @1725
RPM for 5 minutes followed by mixing in an orbital Ross mixer @1725 RPM for 40 minutes
while holding a vacuum @26mm Hg or more. The composition was then steam sterilization
at 121°C for times ranging from 3 minutes to 12 minutes. In addition, one sample was
sterilized for time intervals between 3 minutes and 12 minutes @121°C. Results are
shown in FIG. 21 where G' represents the elastic modulus, G" represents the viscous
modulus and η the complex viscosity. The profile shows that G' and G" intersect at
1.158Hz (7.2 rad/sec). Above this frequency, the composition exhibits non-Newtonian
solution characteristics (tan δ < 1.0). The addition of glycerin to sodium CMC gel
in potassium phosphate significantly affects the rheology of the composition, changing
it from a fundamentally Newtonian fluid to a non-Newtonian fluid above a frequency
of about 1.0.
Example 13
Preparation of 2.8% sodium CMC gel in potassium phosphate buffer and glycerin
[0117] Sodium carboxymethylcellulose was prepared in sterile 25mM to 100mM potassium phosphate
buffer adjusted to a pH of from about 7.2 to about 8.0 using potassium hydroxide and
containing up to 1% glycerin. The dispersion was mixed in an orbital Ross mixer @1725
RPM for 5 minutes followed by mixing in an orbital Ross mixer @1725 RPM for 40 minutes
while holding a vacuum @26mm Hg or more. The composition was then steam sterilization
at 121°C for times ranging from 3 minutes to 12 minutes. In addition, one sample was
sterilized for time intervals between 3 minutes and 12 minutes @121°C. Results are
shown in FIG. 22 where G' represents the elastic modulus, G" represents the viscous
modulus and η the complex viscosity. The profile shows that G' and G" intersect at
0.914Hz (5.7 rad/sec). Above this frequency, the composition exhibits non-Newtonian
solution characteristics (tan δ < 1.0). The addition of glycerin to sodium CMC gel
in potassium phosphate significantly affects the rheology of the composition, changing
it from a fundamentally Newtonian fluid to a non-Newtonian fluid above a frequency
of about 1.0.
Example 14
Preparation of 2.9% sodium CMC gel in potassium phosphate buffer and glycerin.
[0118] Sodium carboxymethylcellulose was prepared in sterile 25mM to 100mM potassium phosphate
buffer adjusted to a pH of from about 7.2 to about 8.0 using potassium hydroxide and
containing up to 1% glycerin. The dispersion was mixed in an orbital Ross mixer @1725
RPM for 5 minutes followed by mixing in an orbital Ross mixer @1725 RPM for 40 minutes
while holding a vacuum @ 26mm Hg or more. The composition was then steam sterilization
at 121°C for times ranging from 3 minutes to 12 minutes. In addition, one sample was
sterilized for time intervals between 3 minutes and 12 minutes @121°C. Results are
shown in FIG. 23 where G' represents the elastic modulus, G" represents the viscous
modulus and η the complex viscosity. The profile shows that G' and G" intersect at
1.065Hz (6.7 rad/sec). Above this frequency, the composition exhibits non-Newtonian
solution characteristics (tan δ < 1.0). The addition of glycerin to sodium CMC gel
in potassium phosphate significantly affects the rheology of the composition, changing
it from a fundamentally Newtonian fluid to a non-Newtonian fluid above a frequency
of about 1.0.
Example 15
1150 C sintered materials include the following materials and process conditions:
[0119] Materials of this exampled included implants having: 30% to 45% Media; 2.6% to 3.25%
CMC; 0 to 15% glycerin; 0mM to 100mM PBS.
[0120] The CMC, buffer, glycerin and media were added together and mixed with a planetary
mixer for 20 minutes to 3 hours under continuous and sustained vacuum. Materials were
filled into 1 cc syringes, pouched in aluminum foil and terminally steam sterilized
@121 C for 15 min to 30 minutes.
[0121] The rheology evaluation was carried out on 30% and 40% media, 2.6% CMC to 3.25% CMC,
1.5% to 15% glycerin, 0 to 25mM. The results of which are shown in FIGS. 24-28. The
materials tested and some of their properties are listed in Table A below. The first
column implant is that as taught in prior art. The second column implant is in accordance
with the principles of the present invention for use in high mobility tissues. The
third column implant is also in accordance with the principles of the present invention,
but for usage in higher bulking required tissues situations where contour shaping
and the filling is of principle concern.
Table A
| Physical parameters/ Material composition |
30% CaHA-3.25 CMC; 15% glycerin |
30% CaHA-2.6% CMC; 1.5% glycerin |
40% CaHA-2.6% CMC; 1.5% glycerin |
| Osmolality (mmol/kg) |
1768 to 2300 |
291 |
289 |
| Extrusion Force (lbf, 0.5" 27 Ga.) |
6.1 |
5.4 |
4.8 |
| Extrusion Force (lbf, 1.25" 27 Ga.) |
11.5 |
9.8 |
7.6 |
| Viscosity (η @0.5Hz) |
413750 |
202865 |
396585 |
| Tan δ @0.5Hz |
0.453 |
0.595 |
0.581 |
| Viscosity modulus (G" @0.5Hz) |
1478.60 |
678.32 |
1331.8 |
| Loss Modulus (G' @0.5Hz) |
671.69 |
404.30 |
773.23 |
[0122] FIG. 24 illustrates the viscosities for each of the materials as shear rate varies.
FIG. 25 illustrates the loss modulus for each of the materials as sheer rate varies.
FIG. 26 illustrates the viscosity modulus for each of the materials as sheer rate
varies. FIG. 27 illustrates the δ for each of the materials as sheer rate varies.
[0123] Material is shear thinning. Varying the gel composition concentrations within the
gel carrier, offers the potential to mimic other rheological variables at higher %
particle medias. Degradation rates of the particles can be manipulated through formulation
in gel rheology. The descriptive characteristics of viscosity and elasticity can be
varied or maintained through gel composition concentrations. The lower viscosity modulus
G" and loss modulus G' the more similar in magnitude to physiological tissues studies
and further asserts the improved biocompatibility not previously reported in prior
art.
[0124] The time dependency of the elasticity is demonstrated in FIG. 28 for varying gel
compositions with varying concentrations of particles. 30% & 40% solids in 2.6 CMC:
1.5% glycerin carrier vs. 30% solids in a 3.25% CMC: 15% glycerin carrier. The material
demonstrates a time dependency to material break down due to composition. The material
with less particles and lower viscosity gels have less tendency to withstand material
stresses.
Example 16
[0125] Alginate/CMC carrier with glycerin was combined with CaHa particles which were sintered
at 1150°C and include the following constitutents (Table B). Various alginate types
have been tested and a summary of the alginates is set forth below in Table B.
Table B
| Alginate (LVM, MVM, M=G, MVG and LVG) |
| Alginate Type |
Guluronic Acid % Mannuronic acid (%) |
Definition |
| LVM |
30-35/65-70 |
Low visocosity alginate gel with high mannuronic acid content.. |
| MVM |
35-45/55-65 |
Medium viscosity alginate gel with high mannuronic acid content. |
| M=G |
45-55/45-55 |
High viscosity alginate gel similar in mannuronic and guluronic acid contents. |
| MVG |
65-75/25-35 |
Low viscosity alginate gel that is cold soluble and has a high guluronic acid content. |
| LVG |
65-75/25-35 |
Very low viscosity alginate gel with high guluronic acid content. |
[0126] M087052: was composed of 30% Media, 40mg/ml to 100mg/ml alginate: 7.5mg/ml to 12.5
mg/ml, 25mM PBS, and 1.5% glycerin.
[0127] The following Alginate/CMC gel formulations (mg/mL) were prepared using the process
detailed below:
[0128] The Alginate/CMC, buffer, glycerin were added together and mixed for 20 min to 3
hours. Particles were then added in 30% by volume and mixed for 20 min to 3 hours.
Materials were filled into 1 cc syringes, pouched in aluminum foil and terminally
steam sterilized @121°C for 1 min to 30 mins.
[0129] Rheological evaluation for these materials are illustrated in the FIGS. 29 and 30.
FIG. 29 illustrates the loss modulus G', the elastic modulus G" and tan δ (G'/G").
FIG. 30 illustrates viscosity and tan δ properties.
Example 17
[0130] Alginate (MVM, M=G or LVM - Various alginates/CMC gels were prepared and include
the following constituents and processes:
[0131] G094035: 5mg/ml to 100mg/ml alginate (MVM, M=G or LVM (see Table B)): 2.5mg/ml to
50 mg/ml CMC, 25mM PBS, 1.5% glycerin. The following Alginate/CMC gel formulations
(mg/mL) were prepared using the process detailed below:
[0132] The Alginate/CMC, buffer, glycerin were added together and mixed for 20 min to 3
hours with either an orbital rotatary mixer or direct propeller mixer. Materials were
filled into 1 cc syringes, pouched in aluminum foil and terminally steam sterilized
@121°C for 15 min to 30 mins.
Example 18
[0133] In one embodiment, the implant may be designed for application in the laryngeal tissue.
Table C lists the parameters for such an implant.
Table C
| Specification |
Laryngeal Implant |
| Viscosity |
107,620 - 517,590 cps. |
| Osmolarity |
255 mOs to 327 mOs |
| pH |
7.0±1.0 |
| Loss on Drying |
-29.7% to -43.1 %. |
| Percent Solids |
54.3 to 70.5% |
| Extrusion Force |
3.60 - 7.20 lbsf |
Example 19
[0134] The prediction model was developed using the SAS JMP ver 7.0 statistical software.
The prediction model data used the screening model's graphing scripts, which are mathematical
equations of the surface contours of the models. These can be obtained by highlighting
the model output and saving the response prediction formula to a data spreadsheet.
Values populated the screening model with model outputs for the screening model inputs
tested. The prediction model formulae were then exported to a separate spreadsheet,
where a full factorial model design was developed. In one case, for example, the following
optimized parameters based on the screening model were used: Sterilization (121°C)
F0 22, 25, 28, and 33 respectively. The CMC concentration (%CMC) was varied between
2.3% w/v and 2.9% w/v in 0.1% w/v increments. The glycerin concentration (%gly) was
held to 0% w/v, 1.0% w/v and 1.5% w/v. The buffer concentration (mM) was varied from
0.25mM, 50mM and 100mM concentration. The model was populated with the screening model
prediction formula outputs representing 625 individual runs. This then represents
the whole prediction model using optimized sterilization inputs based on the same
inputs for the screening model previously conducted. The model was then re-evaluated
over the same output parameters using the Simulator function with 10000 runs.
[0135] Simulation allows the determination of the distribution of model outputs as a function
of the random variation in the factors and model noise. The simulation facility in
the profilers provides a way to set up the random inputs and run the simulations,
producing an output table of simulated values. In this application the boundary conditions
are estimated by the defect rate of a process that has been fit to specific rheological
parameters to determine if it is robust with respect to variation in the factors.
If specifications have been set in the response, they are carried over into the simulation
output, allowing a prospective boundary analysis of the simulated model variable using
new factors settings. In the Profiler function, the Simulator function is integrated
into the graphical layout. Factor specifications are aligned below each factor's profile.
A simulation histogram is shown in FIG. 9B on the right for each response.
[0136] Factors (inputs) and response (outputs) are already given roles by being in the Profiler.
Additional specifications for the simulator are including assigning random values
to the factors and adding random noise to the responses.
[0137] For each factor, the assignment of values is important. The Random program assigns
the factor a random value with the specified distributon and distributional parameters.
[0138] Normal truncated is a normal distribution limited by lower and upper limits. Any
random realization that exceeds these limits is discarded and the next variate within
the limits is chosen. This is used to simulate an inspection system where inputs that
do not satisfy specification limits are discarded or sent back.
[0139] The Add Random Noise function obtains the response by adding a normal random number
with the specified standard to the evaluated model.
[0140] The Defect Profiler function shows the defect rate as an isolated function of each
factor. This command is enabled when specification limits are available, as described
below.
[0141] The Profiler function displays profile traces. A profile trace is the predicted response
as one variable is changed while the others are held constant at the current values.
The Profiler re-computes the profiles and provides predicted responses (in real time)
as the value of an X variable is varied. The vertical dotted line for each X variable
shows its current value or current setting.
[0142] For each X variable, the value above the factor name is its current value.
[0143] The horizontal dotted line shows the current predicted value of each Y variable for
the current values of the X variables.
[0144] The black lines within the plots of FIG. 9B show how the predicted value changes
when the current value of an individual X variable is changed. In fitting platforms,
the 95% confidence interval for the predicted values is shown by a dotted blue curve
surrounding the prediction trace (for continuous variables) or the context of an error
bar (for categorical variables).
[0145] The Profiler is then a way of changing one variable at a time and looking at the
effect on the predicted response.
[0146] There are several important points to note when interpreting a prediction profile:
[0147] 1. The importance of a factor can be assessed to some extent by the steepness of
the prediction trace. If the model has curvature terms (such as squared terms), then
the traces may be curved.
[0148] 2. If you change a factor value, then its prediction trace is not affected, but the
prediction traces of all the other factors can change. The Y response line must cross
the intersection points of the prediction traces with their current value lines.
[0149] 3. Note: If there are interaction effects or cross-product effects in the model,
the prediction traces can shift their slope and curvature as you change current values
of other terms. That is what interaction is all about. If there are no interaction
effects, the traces only change in height, not slope or shape.
[0150] Prediction profiles are especially useful .in multiple-response models to help judge
which factor values can optimize a complex set of criteria.
[0151] The Profiler shows the confidence bars on the prediction traces of continuous factors,
along with the sensitivity Indicator displayed in triangles, whose height and direction
correspond to the value of the derivative of the profile function at its current value.
This is useful in large profiles to be able to quickly spot the sensitive cells.
[0152] The prime reason to make random factor tables is to explore the factor space in a
multivariate way using graphical queries. This technique is called Filtered Monte
Carlo. This allows visualization of the locus of all factor settings that produce
a given range to desirable response settings. By selecting and hiding the points that
do not qualify (using graphical brushing or the Data Filter), the remaining opportunity
space yields the result desired.
[0153] The Simulator enables the creation of Monte Carlo simulations using random noise
added to factors and predictions for the model. Fixed factors were set over a range
of settings and allowed for 1 s.d of model noise to random values to determine the
rate that the responses are outside the specification limits.
[0154] Often there are multiple responses measured for each set of experimental conditions,
and the desirability of the outcome involves several or all of these responses. For
example, one response can be maximized while another is minimized, and a third response
kept close to some target value. In desirability profiling, a desirability function
is specified for each response. The overall desirability can be defined as the geometric
mean of the desirability for each response.
[0155] The Desirabiltiy Profiler function components and examples of desirability functions
settings are discussed next. The desirability functions are smooth piecewise functions
that are crafted to fit the control points.
[0156] The minimize and maximize functions are three-part piecewise smooth functions that
have exponential tails and a cubic middle.
[0157] The target function is a piecewise function that is a scale multiple of a normal
density on either side of the target (with different curves on each side), which is
also piecewise smooth and fit to the control points.
[0158] These choices give the functions good behavior as the desirability values switch
between the maximize, target, and minimize values.
[0159] The control points are not allowed to reach all the way to zero or one at the tail
control points.
[0161] The default desirability function setting is maximize ("higher is better"). The top
function handle is positioned at the maximum Y value and aligned at the high desirability,
close to 1. The bottom function handle is positioned at the minimum Y value and aligned
at a low desirability, close to 0.
[0163] A target value can be designated as "best." In this example, the middle function
handle is positioned at Y = 55 and aligned with the maximum desirability of 1. Y becomes
less desirable as its value approaches either 70 or 42. The top and bottom function
handles at Y = 70 and Y = 42 are positioned at the minimum desirability close to 0.
[0165] The minimize ("smaller is better") desirability function associates high response
values with low desirability and low response values with high desirability. The curve
is the maximization curve flipped around a horizontal line at the center of plot.
[0166] The Desirability Profile
[0167] The last row of plots in FIG. 9B shows the desirability trace for each response.
The numerical value beside the word Desirability on the vertical axis is the geometric
mean of the desirability measures. This row of plots shows both the current desirability
and the trace of desirabilities that result from changing one factor at a time.
[0168] Desirability Profiling for Multiple Responses
[0169] A desirability index becomes especially useful when there are multiple responses.
[0170] Defect Rate Function
[0171] The defect rate shows the probability of an out-of-specification output defect as
a function of each factor, while the other factors vary randomly. This is used to
help visualize which factor's distributional changes the process is most sensitive
to, in the quest to improve the description of the boundary functions.
[0172] Specification limits define what is a defect, and random factors provide the variation
to produce defects in the simulation. Both need to be present for a Defect Profile
to be meaningful.
[0173] The institution of a lower limit acceptable desirability is appropriate since analysis
is based on finite data sampling and the lower limit was instituted to be values greater
than 0.15. Based on those limitations, the whole simulation model has the following
limiting parameters as follows.
FO=24 to 35
PBS = 22mM to 140mM
% CMC = 2.3% w/v to 3.3% w/v
%Glycerin= 0.3% w/v to 2.5 w/v
[0174] However, individual experimentation has identified limiting parameters that are most
favorable for producing the outputs within the specification range, while maintaining
a sterile product. Their conditions are as follows:
FO = 22 to 30
PBS = 25mM to 100mM
% CMC = 2.3% w/v to 2.9% w/v
% Glycerin = 0% w/v to 1.5% w/v
[0175] An example of the 2D and 3D plots which result are shown in FIGS. 31A-31F. These
figures show the evaluation of the desirability function expressed as a function two
of the following design inputs: %CMC, Fo; % glycerin and PBS.. The boundary limiting
condition for the percent CMC vs. Fo is defined by the 0.7Hz tan δ contour trace from
2.3 to 2.7. The 2D plot shows a white region within which the rheological parameter
is met and is consistent with the desirability function shown in FIG. 9B.
[0176] The model trace formulae for the whole model are as follows for the following outputs.
[0177] Prediction Formula Viscosity 0.7Hz :
(-0.0662001910451557) + 0.051920253378124 * :Fo + 0.0146791342721163 * :Name("PBS
(mM)") + -0.218700904653452 * :Name("% NaCMC") + -0.0202956176083598 * :Name(% Glycerin")
+ (:Fo - 22.0003631356491) * ((:Fo - 22.0003631356491) * -0.00371533851417633) + (:Fo
-22.0003631356491) * ((:Name("PBS (mM)") - 63.5057099845838) * 0.000185185074554069)
+ (:Name("PBS (mM)") - 63.5057099845838) * ((:Name("PBS (mM)") - 63.5057099845838)
* -0.0000863865657255508) + (:Fo - 22.0003631356491) * ((:Name("% NaGMC") - 2.85245995014651)
* -0.0322726861725922) + (:Name("PBS (mM)") - 63.5057099845838) * ((:Name("% NaCMC")
- 2.85245995014651) * -0.0152609626718641) + (:Name("% NaCMC") - 2.85245995014651)
* ((:Name("% NaCMC") - 2.85245995014651) * 0.942295293128045) + (:Fo - 22.0003631356491)
* ((:Name("% Glycerin") - 1.49703269551474) * 0.0048399350260245) + (:Name("PBS (mM)")
- 63.5057099845838) * ((:Name("% Glycerin") - 1.49703269551474) * 0.00387275533427914)
+ (:Name("% NaCMC") - 2.85245995014651) * ((:Name("% Glycerin") - 1.49703269551474)
* - 0.213067717437202) + (:Name("% Glycerin") - 1.49703269551474) * ((:Name("% Glycerin")
- 1.49703269551474) * 0.052309021299775)
[0178] Prediction Formula Tan δ 0.7Hz:
(-0.0662001910451557) + 0.051920253378124 * :Fo + 0.0146791342721163) * :Name("PBS
(mM)") + -0.218700904653452 * :Name("% NaCMC") + -0.0202956176083598 * :Name("% Glycerin")
+ (:Fo - 22.0003631356491) * ((:Fo - 22.0003631356491) * -0.00371533851417633) + (:Fo
- 22.0003631356491) * ((:Name("PBS (mM)") - 63.5057099845838) * 0.000185185074554069)
+ (:Name("PBS (mM)") - 63.5057099845838) * ((:Name("PBS (mM)") - 63.5057099845838)
* -0.0000863865657255508) + (:Fo - 22.0003631356491) * ((:Name("% NaCMC") - 2.85245995014651)
* -0.0322726861725922) + (:Nanne("PBS (mM)") - 63.5057099845838) * ((:Name("% NaCMC")
- 2.85245995014651) * -0.0152609626718641) + (:Name("% NaCMC") - 2.85245995014651)
* ((:Name("% NaCMC") - 2.85245995014651) * 0.942295293128045) + (:Fo - 22.0003631356491)
* ((:Name("% Glycerin") - 1.49703269551474) * 0.0048399350260245) + (:Name("PBS (mM)")
- 63.5057099845838) * ((:Name("% Glycerin") - 1.49703269551474) * 0.00387275533427914)
+ (:Name("% NaCMC") - 2.85245995014651) * ((:Name("% Glycerin") - 1.49703269551474)
* - 0.213067717437202) + (:Name("% Glycerin") - 1.49703269551474) * ((:Name("% Glycerin")
- 1.49703269551474) * 0.052309021299775)
[0179] Prediction Formula G' 0.7Hz :
65.1530428282072 + -4.56421653385048 * :Fo + -1.24220316891102 * : Name("PBS (mM)")
+ 53.0767618580076 * :Name("% NaCMC") + 9.296089270897 * :Name("% Glycerin") + (:Fo
- 22.0003631356491) * ((:Fo - 22.0003631356491) * 0.185460632264244) + (:Fo - 22.0003631356491)
* ((:Name("PBS (mM)") - 63.5057099845838) * 0.0152064998484757) + (:Name("PBS (mM)")
- 63.5057099845838) * ((:Name("PBS (mM)") - 63.5057099845838) * 0.0121675367725622)
+ (:Fo - 22.0003631356491) * ((:Name("% NaCMC") - 2.85245995014651) * - 1.59402906490529)
+ (:Name("PBS (mM)") - 63.5057099845838) * ((:Name("% NaCMC") - 2.85245995014651)
* -0.82120066059178) + (:Name("% NaCMC") - 2.85245995014651) * ((:Name("% NaCMC")
- 2.85245995014651) * - 3.41806241403989) + (:Fo - 22.0003631356491) * ((:Name("%
Glycerin") - 1.49703269551474) * -0.194222622094197) + (:Name("PBS (mM)") - 63.5057099845838)
* ((:Name("% Glycerin") - 1.49703269551474) * - 0.237225958870055) + (:Name("% NaCMC")
- 2.85245995014651) * ((:Name("% Glycerin") - 1.49703269551474) * - 0.363919647719381)
+ (:Name("% Glycerin") - 1.49703269551474) * ((:Name("% Glycerin") - 1.49703269551474)
* -0.960279042125364)
[0180] Prediction Formula G" 0.7Hz:
42.340284211014 + -4.44571705075887 * :Fo + -0.951595662768327 * :Name("PBS (mM)")
+ 57.6631139101727 * :Name("% NaCMC") + 4.93958206506618 * :Name("% Glycerin") + (:Fo
- 22.0003631356491) * ((:Fo - 22.0003631356491) * 0.1897777224472) + (:Fo - 22.0003631356491)
* ((:Name("PBS (mM)") - 63.5057099845838) * 0.00526490794925264) + (:Name("PBS (mM")
- 63.5057099845838) * ((:Name("PBS (mM)") - 63-5057099845838) * 0.00750944190873103)
+ (:Fo - 22.0003631356491) * ((:Name("% NaCMC") - 2.85245995014651) * - 1.59674778661272)
+ (:Name("PBS (mM)") - 63.5057099845838) * ((:Name("% NaCMC") - 2.85245995014651)
* -0.55449874562251) + (:Name("% NaCMC") - 2.85245995014651) * ((:Name("% NaCMC")
- 2.85245995014651) * 17.0085346258082) + (:Fo - 22.0003631356491) * ((:Name("% Glycerin")
- 1.49703269551474) * -0.0425836269658459) + (:Name("PBS (mM)") - 63.5057099845838)
* ((:Name("% Glycerin") - 1.49703269551474) * - 0.187414471985777) + (:Name("% NaCMC")
- 2.85245995014651) * ((:Name("% Glycerin") - 1.49703269551474) * - 2.3241038908658)
+ (:Name("% Glycerin") - 1.49703269551474) * ((:Name("% Glycerin") - 1.49703269551474)
* -0.73370622281908)
[0181] Prediction Formula Tan δ 4Hz
9.45512533634532 + -0.126696086121843 * :Fo + -0.00117658850182967 * :Name("PBS (mM)")
+ -2.00308587650446 * :Name("% NaCMC") + 0.165674034118311 * :Name("% Glycerin") +
(:Fo - 22.0003631356491) * ((:Fo - 22.0003631356491) * 0.00365527346963407) + (:Fo
- 22.0003631356491) * ((:Name("PBS (mM)") - 63.5057099845838) * 0.000511204818741645)
+ (:Name("PBS (mM)")- 63.5057099845838) * ((:Name("PBS (mM)") - 63.5057099845838)
* 0.0000499689391927876) + (:Fo - 22.0003631356491) * ((:Name("% NaCMC") - 2.85245995014651)
* -0.0624166549775326) + (:Name("PBS (mM)") - 63.5057099845838) * ((:Name("% NaCMC")
- 2.85245995014651) * 0.0199800709717944) + (:Name("% NaCMC") - 2.85245995014651)
* ((:Name("% NaCMC") - 2.85245995014651) * - 8.94890476212236) + (:Fo - 22.0003631356491)
* ((:Name("% Glycerin") - 1.49703269551474) * -0.0266258304941918) + (:Name("PBS (mM)")
- 63.5057099845838) * ((:Name("% Glycerin") - 1.49703269551474) * - 0.0159932411399036)
+ (:Name("% NaCMC") - 2.85245995014651) * ((:Name("% Glycerin") - 1.49703269551474)
* 1.21969695165947) + (:Name("% Glycerin") 1.49703269551474) * ((:Name("% Glycerin")
- 1.49703269551474) 0.00451334325524632)
[0182] Prediction Formula G' 4.0Hz
119.421921614245 + -12.2323465265668 * :Fo + -2.68101314812006 * : Name("PBS (tnM)")
+ 146.999647742916 * :Name("% NaCMC") + 27.8854022682617 * :Name("% Glycerin") + (:Fo
- 22.0003631356491) * ((:Fo - 22.0003631356491) * 0.519903664055683) + (:Fo - 22.0003631356491)
* ((:Name("PBS (mM)") - 63.5057099845838) * 0.0209551675180216) + (:Name("PBS (mM)")
- 63.5057099845838) * ((:Name("PBS (mM)") - 63.5057099845838) * 0.0232180450227683)
+ (:Fo - 22.0003631356491) * ((:Name("% NaCMC") - 2.85245995014651) * - 3.12498688301935)
+ (:Name("PBS (mM)") - 63.5057099845838) * ((:Name("% NaCMC") - 2.85245995014651)
* -1.68010649138557) + (:Name("% NaCMC") - 2.85245995014651) * ((:Name("% NaCMC")
- 2.85245995014651) * 47.7871554829216) + (:Fo - 22.0003631356491) * ((:Name("% Glycerin")
- 1.49703269551474) * -0.520125030291254) + (:Name("PBS (mM)") - 63.5057099845838)
* ((:Name("% Glycerin") - 1.49703269551474)*-0.516575698317358) + (:Name("% NaCMC")
- 2.85245995014651) * ((:Name("% Glycerin") - 1.49703269551474) * 7.81902442047261)
+ (:Name("% Glycerin") - 1.49703269551474) * ((:Name("% Glycerin") - 1.49703269551474)
* -2.08529318048302)
[0183] Prediction Formula G" 4.0Hz
9.16270416349258 + -6.65052721006341 * :Fo + -1.30157689213324*: Name("PBS (mM)" )
+ 113.264274857613 * :Name("% NaCMC") + 12.6630272567578 * :Name("% Glycerin") + (:Fo
- 22.0003631356491) * ((:Fo - 22.0003631356491) * 0.278888472140156) + (:Fo - 22.0003631356491)
* ((:Name("PBS (mM)") - 63.5057099845838) * - 0.00310223504985895) + (:Name("PBS (mM)")
- 63.5057099845838) * ((:Name("PBS (mM)") - 63.5057099845838) * 0.00757715798304363)
+ (:Fo - 22.0003631356491) * ((-Name("% NaCMC") - 2.85245995014651) * - 1.30849884761416)
+ (:Name("PBS (mM)") - 63.5057099845838) * ((:Name("% NaCMC") - 2.85245995014651)
* -0.702979541219968) + (:Name("% NaCMC")-2.85245995014651) * ((:Name("% NaCMC") -
2.85245995014651) * 57.4260758452326) + (:Fo - 22.0003631356491) * ((:Name("% Glycerin")
- 1.49703269551474) * -0.140690664543388) + (:Name("PBS (mM)") - 63.5057099845838)
* ((:Name("% Glycerin") - 1.49703269551474) * - 0.221880322555676) + (:Name("% NaCMC")
- 2.85245995014651) * ((:Name("% Glycerin") - 1.49703269551474) * 3.07273854570663)
+ (:Name("% Glycerin") - 1.49703269551474) * ((:Name("% Glycerin") - 1.49703269551474)
* -1.0565937205507)
[0184] Prediction Formula PF d-R 0.7Hz
78.8594056631251 + -0.391595419225251 * :Fo + 0.194490163649969* : Name("PBS (mM)")
+ -9.00551677919371 * :Name("% NaCMC") + - 1.31216569248401 * :Name("% Glycerin")
+ (:Fo - 22.0003631356491) * ((:Fo - 22.0003631356491) * 0.0397402622686809) + (:Fo
- 22.0003631356491) * ((:Name("PBS (mM)") - 63.5057099845838) * 0.00616186280104159)
+ (:Name("PBS (mM)") - 63.5057099845838) * ((:Name("PBS (mM)") - 63.5057099845838)
* -0.00101989657856309) + (:Fo - 22.0003631356491) * ((:Name("% NaCMC") - 2.85245995014651)
* - 0.843405024379471) + (:Name("PBS (mM)") - 63.5057099845838) * ((:Name("% NaCMC")
- 2.85245995014651) * -0.103279939139173) + (:Name("% NaCMC") - 2.85245995014651)
* ((:Name("% NaCMC") - 2.85245995014651) * - 22.9264118725924) + (:Fo - 22.0003631356491)
* ((:Name("% Glycerin") - 1.49703269551474) * -0.0439660358574415) + (:Name("PBS (mM)")
- 63.5057099845838) * ((:Name("% Glycerin") - 1.49703269551474) * - 0.0619122070598477)
+ (:Name("% NaCMC") - 2.85245995014651) * ((:Name("% Glycerin") - 1.49703269551474)
* 10.1261963249863) + (:Name("% Glycerin") - 1.49703269551474) * ((:Name("% Glycerin")-1.49703269551474)
* 0.34697984176467)
[0185] Prediction Formula PF d-R 0.7Hz
78.8594056631251 + -0.391595419225251 * :Fo + 0.194490163649969 * : Name("PBS (mM)")
+ -9.00551677919371 * :Name("% NaCMC" ) + - 1.31216569248401 * :Name("% Glycerin")
+ (:Fo - 22.0003631356491) * ((:Fo - 22.0003631356491) * 0.0397402622686809) + (:Fo
- 22.0003631356491) * ((:Name("PBS (mM)") - 63.5057099845838) * 0.00616186280104159)
+ (:Name("PBS (mM)") - 63.5057099845838) * ((:Name("PBS (mM)") - 63.5057099845838)
* -0.00101989657856309) + (:Fo - 22.0003631356491) * ((:Name("% NaCMC") - 2.85245995014651)
* - 0.843405024379471) + (:Name("PBS (mM)") - 63.5057099845838)* ((:Name("% NaCMC")
- 2.85245995014651) * -0.103279939139173) + (:Name("% NaCMC") - 2.85245995014651)
* ((:Name("% NaCMC") - 2.85245995014651) * - 22.9264118725924) + (:Fo - 22.0003631356491)
* ((:Name("% Glycerin") - 1.49703269551474) * -0.0439660358574415) + (:Name("PBS (mM)")
- 63.5057099845838) * ((:Name("% Glycerin") - 1.49703269551474) * - 0.0619122070598477)
+ (:Name("% NaCMC") - 2.85245995014651) * ((:Name("% Glycerin") - 1.49703269551474)
* 10.1261963249863) + (:Name("% Glycerin") - 1.49703269551474) * ((:Name("% Glycerin")
- 1.49703269551474) * 0.34697984176467)
Example 20
[0186] This example consists of the screening model's 59 independent runs of conditions
with rheological outputs registered and see following data Tables D and E:
Table D
| Output |
Min |
Max |
| |
|
|
| Viscosity η* (0.7Hz, 30τ, 30°C) |
7200 |
53000 |
| Tan δ (0.7Hz, 30τ, 30°C) |
.6 |
1.5 |
| G' elastic modulus, G" viscosity Modulus (0.7Hz, 30τ, 30°C) |
|
100 |
| Tan δ (4Hz, 30τ, 30°C) |
0.3 |
2 |
| G' elastic modulus, G" viscosity Modulus (4Hz, 30τ, 30°C) |
|
300 |
| Phase Angle δ-R (0.7Hz, 30τ, 30°C) |
|
60 |
| Phase Angle δ-R (0.7Hz, 30τ, 30°C) |
|
110 |
Example 20
[0187]

[0188] Although the present invention has been described with reference to preferred embodiments,
one skilled in the art can easily ascertain its essential characteristics and without
departing from the spirit and scope thereof, can make various changes and modifications
of the invention to adapt it to various usages and conditions. Those skilled in the
art will recognize or be able to ascertain using no more than routine experimentation,
various reasonable equivalents to the specific embodiments of the invention herein.
Such equivalents are to be encompassed in the scope of the present invention. For
example, the plasticizer utilized in the examples of the present invention is primarily
glycerin. However, one of ordinary skill in the art would appreciate that other plasticizers
may be used without departing from the spirit and scope of the invention.
In view of the foregoing, it will be appreciated that the invention described herein
inter alia relates to the following items:
1. A method of preparing an implant with a desired rheological property selected to
be compatible with at least one tissue rheological feature and at least one acceptable
tissue rheological range at a tissue site of implantation, the method comprising:
establishing at least one of a particular rheological feature and an acceptable rheological
range characteristic of the tissue at the tissue implantation site;
identifying an implant having at least one of the at least one particular rheological
feature and the acceptable range; and
preparing the implant having the desired rheological property.
2. The method as defined in Item 1 wherein the step of identifying an implant with
the at least one particular rheological feature and acceptable rheological range comprises;
collecting data for a plurality of test implants, the data being characteristic of
chemical variables and rheological variables for each of the plurality of test implants;
and
mapping the data to define at least one of characteristic phase lines and characteristic
closed phase region which meet the at least one particular rheological feature and
acceptable rheological range for the rheological property
3 The method as defined in Item 1 wherein the step of mapping the data comprises establishing
the characteristic closed phase region within which a plurality of the chemical variables
provide the implant having a plurality of associated rheological properties compatible
with the tissue at the implantation site.
4. The method as defined in Item 1 wherein the step of identifying an implant includes
establishing sensitivity of changes in the rheological property of the implant as
a function of change in chemical variables.
5. The method as defined in Item 1 further including the step of establishing statistical
boundaries for at least one of the characteristic phase lines and the characteristic
closed phase region.
6. The method as defined in Item 1 wherein the particular rheological feature comprises
a cross-over of functionality of G' and G".
7. The method as defined in item 1 wherein the rheological property comprises compatibility
of phase angle versus frequency for the implant and the tissue.
8. The method as defined in Item 1 wherein the implant comprises a polysaccharide
polymer.
9. The method as defined in Item 1 wherein the implant comprises a polysaccharide
polymer having an Fo value of at least about 22.
10. The method of Item 9, wherein the polysaccharide polymer is selected from the
group consisting of an alginate polysaccharide, a cellulose polysaccharide and a hemicellulose
polysaccharide.
11. The method of Item 9, wherein the cellulose based polysaccharide polymer is selected
from the group consisting of: sodium carboxymethylcellulose, hydroxyethyl cellulose,
ethylhydroxyethyl cellulose, carboxymethyl cellulose, carboxyethylhydroxyethyl cellulose,
hydroxypropylhydroxyethyl cellulose, methyl cellulose, methylhydroxylmethyl cellulose,
methylhydroxyethyl cellulose, carboxymethylmethyl cellulose, and modified derivatives
thereof.
12. The method as defined in Item 1 wherein the step of preparing the implant includes
addition of a buffer.
13. The method of Item 12 wherein the buffer comprises a potassium phosphate.
14. The method as defined in Item 1 wherein the step of preparing the implant includes
adding a lubricant.
15. The method as defined in Item 14 wherein the lubricant comprises glycerin.
16. The method as defined in Item 1 wherein the step of preparing the implant comprises
adding particles.
17. The method as defined in Item 16 wherein the particles comprise a ceramic.
18. The method as defined in Item 17 wherein the ceramic particles have a size range
of about 20 to 200 microns and have a volume percent of about 5 to 65 percent.
19. A tissue implant product for a tissue site comprising:
a polysaccharide polymer having an Fo value between about 22 and 34 and a buffer component,
wherein rheology parameters of the implant product include a cross-over of G' and
G" and phase frequency functionality of the implant product exhibits a behavior in
three regions of tissue functionality of the same category as the tissue site.
20. The tissue implant product as defined in Item 19 further including the feature
that phase frequency functionality of the implant product exhibits a behavior in three
regions of tissue functionality of the same category as the tissue site.
21. The tissue implant product as defined in Item 19 further including a rheological
feature requirement for the implant product of being within a phase region meeting
a plurality of rheological parameters characteristic of the tissue site.
22. An implant having a rheological properly selected to be compatible with tissue
at an implant site, prepared in accordance with a method comprising the steps of:
establishing at least one required rheological feature for the tissue at the implant
sites;
identifying an implant having the required rheological feature; and
preparing the implant having the required rheological feature so as to be compatible
with the tissue at the implant site.
23. The implant as defined in Item 22 wherein the steps of identifying an implant
includes establishing at least one chemical variable associated with the required
rheological feature.
24. The implant as defined in Item 22 wherein the step of identifying an implant having
the required rheological feature comprises mapping the at least one required rheological
feature versus a plurality of chemical variables to identify a combination of the
chemical variables which enables meeting the at least one required rheological feature.
25. The implant as defined in Item 24 wherein the at least one required rheological
feature comprises G' and G" functional behavior intersecting each other between about
0.1 - 10Hz tissue response.
26. The implant as defined in Item 25 wherein G" is greater than G' until intersection.
27. The implant as defined in Item 24 wherein the step of mapping the at least one
required rheological feature comprises statistical analysis of changing the chemical
variables to establish at least one of a line and a volume of desirability associated
with an implant rheological feature which is compatible with the at least required
rheological feature.
28. A method for identifying an implant for a selected tissue implant site of a particular
type of patient, the method comprising:
a supplier providing a clinician rheological data for tissue of a particular type
of patient at a prospective tissue implant site; and
a clinician reviewing data from the supplier of a plurality of potentially useful
implant products, the data from the supplier providing (a) information on the rheological
properties of each of the plurality of the implant products and (b) further indicating
whether the rheological properties will meet compatibility requirements for the particular
type of patient tissue at the implant site.
29. The method as defined in Item 28 wherein the data from the supplier includes information
on change of a rheological parameters for the implant as a function of change of chemical
variables of the implant.
30. A method of implanting a tissue augmentation product in a patient, comprising
the steps of:
characterizing a tissue in a particular type of patient;
reviewing data from a supplier which includes identifying a tissue augmentation product
having rheological properties compatible with the tissue of the particular type of
patient; and
implanting the tissue augmentation product in the patient in accordance with the data
from the supplier.
31. A method of establishing a treatment protocol for implantation of a tissue augmentation
product which is compatible with a patient tissue site, comprising the steps of:
identifying particular rheological properties associated with tissue of a particular
type of patient;
providing implant rheological data for a plurality of tissue augmentation products;
and
identifying selected tissue augmentation products which have implant rheological data
which is indicative of being compatible with the tissue of the particular type of
patient.
32. The method as defined in Item. 31 wherein the tissue of the particular type of
patient is selected from the group consisting of
vocal fold, nasolabial folds, marionette lines, cheek augmentation, lips, urinary
tract, and wrinkles and folds: